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Synthesis of Biobased Terephthalic Acid: Enabling Manufacture of 100% Renewable PET
1
Sebastien ThueillonKelly Miller
Yukari Nishizawa-BrennenKaren M. DrathsJohn W. Frost
Funding:National Science Foundation
The Coca-Cola Company
Michigan Bioeconomy Institute Holland, MI
February 10, 2016
Poly(ethylene terephthalate)
OHHO
O
O
HO OH
terephthalic acid
ethylene glycol
PTAH2O
OO
O
O
O
npoly(ethylene terephthalate)
Manufacture of Terephthalic Acid
BTX
parafinnic oilnaphthenic oil
Pt/Re on Al2O3 SiO2
H2
400-500oCliquid-liquid extraction UOP Parex
Toray Aromax
HO
O
O
O
OCO2H
CO2H
OHO
O
H2
CO2
HO
OH
OH
OHOH
OH
a b
c
d
e
f
gh
i
j
kl
Biobased Terephthalic Acid
CO2R
RO2C
HO2CCO2H
CO2H
HO2C
CO2CH3
CH3O2C
O
ORO
RO R = HR = CH3
ORO2C
O
CO2CH3
HO2CCO2H
OH
R=CH3 R=H
R=HR=CH3
O
OHO2C
CO2H
OHO
O
CO2CH3
CH3O2C O
O
2
2
a
b
c
d H2 H2O
HO
OH
d
e
f
g
h
CO2H
CO2H
i
j
k
l
H2
• p-Xylene intermediacy - 4 routes • No p-xylene intermediacy – 6 routes• No p-xylene/Amoco MidCentury – 2 routes• No p-xylene/no Amoco MidCentury/esterification/hydrolysis – 2 routes
Alder Reaction Sequence
Alder, K.; Dortmann, H. A. Chem. Ber. 1952, 85, 556-565.
• No esterification followed by ester hydrolysis• Solvent-free cycloaddition reaction• Enables access to both terephthalic acid and isophthalic acid
Cahiez, G.; Rivas-Enterrios, J.; Clery, P. Tetrahedron Lett. 1988, 29, 3659-3662.
(a) cycloaddition; (b/b’) aromatization; (c/c’) oxidation
CO2H
CO2H CO2H
a
CO2H CO2H
b c
b' c'
HO2C
CO2H
HO2C CO2H
para
meta
Bridgestone - Ajinomoto Goodyear - Dupont (the former Genencor)Michelin - Amyris
http://www.icis.com/blogs/green-chemicals/2012/06/ajinomoto-bridgestone-in-bio-i.html
Biobased Isoprene:
Biobased Acrylic Acid:Dow - OPX bio
http://www.slideshare.net/opxbio/opxbio-dow-renewable-route-to-acrylic-acidBASF - Cargill - Novozyme ArkemaMyriant
Starting Materials
Cycloaddition
Lewis Acid Catalysis:• Increase reaction rate by stabilizing the
LUMO of acrylic acid.• Increase para selectivity by perturbing the
orbital coefficients of acrylic acid.-or-
Lewis Acid Catalysis:• Lewis-acid promoted Brønsted acidity of
acrylic acid.• Acid-catalyzed polymerization of isoprene
OH
OMClx OH
OMClxδδ
Miller, K. M.; Zhang, P.; Nishizawa-Brennen, Frost, J. W. ACS Sustainable Chem. Eng. 2014, 2, 2053-2056.
TiCl4-Catalyzed Cycloaddition
TiO
ClClO
O
OTi Cl
ClO
O
O
O H
OH
OH
O TiCl42 mol%neat neat
O
OH
89%para
meta
OH
O4%
?
BOB-Catalyzed Cycloaddition
OB
O
O OB
O
OO
O
O
0.5
0.5
0.5
0.5OHB
HO OH O
O O 110oC
BOB(OAc)4
• Cycloaddition rates 2x faster for BOB(OAc)4 vs. TiCl4.
• BOB(OAc)4 is halide-free.
• BOB(OAc)4 is a crystalline solid.
OB
O
O OB
O
OO
O
O
0.5
0.5
0.5
0.5OH
O2 mol%neat
BOB(OAc)4neat
O
OH
91%para
meta
OH
O5%
Aromatization
Alder 1952, Tong 2014:
CO2H CO2H
para
H2SO4100oC
SO2 79%
a) Alder, K.; Dortmann, H. A. Chem. Ber. 1952, 85, 556-565.b) Wang, F; Tong, Z. RSC Adv. 2014, 4, 6314-6317.
Pd(0) Aromatization
CO2H CO2H
para
H2SO4100oC
SO2 79% meta
H2SO4100oC
SO2 9%CO2H CO2H
CO2H CO2H
para77%
H2
Pd on C 240oC, 0.11bar CO2H
9%
CO2H
12%
Alder 1952, Tong 2014:
meta 69%CO2H CO2H
H2
Pd on C 240oC, 0.11 bar
13%CO2H
10%CO2H
Frost 2014:
Miller, K. M.; Zhang, P.; Nishizawa-Brennen, Frost, J. W. ACS Sustainable Chem. Eng. 2014, 2, 2053-2056.
Pd(0) Aromatization
Management of H-Pd-H:
CO2H
CO2HPdH
CO2HH PdH
Pd(0)
CO2H
cyclohexane byproduct
CO2H
p-toluic acid
H Pd H Pd(0)Pd(0) -H2
+H2H H
Dis$lling bulb
Plug reactor
Receiver bulbs
To water aspirator pump
Pneuma$c actuator
-‐78 °C cold trap
Vapor Phase Aromatization
Oxidation
Alder 1952, Tong 2014:
CO2H
HO2C
CO2HKMnO4
95%
CO2H
HO2C
CO2HMn(OAc)2, Co(OAc)2N-hydroxysuccinimide
O2, HOAc, 100oC94%
Frost 2014:
CO2H HO2C CO2H88%
Mn(OAc)2, Co(OAc)2N-hydroxysuccinimide
O2, HOAc, 100oC
Alder Route to Biobased Terephthalic Acid
Cycloaddition: solvent-free, 2 mol% catalyst, highly selective
Aromatization: solvent-free, vapor-phase, high mass balance
Oxidation: 0.5 mol% catalyst, highly selective
Enabling: Synthesis of both terephthalic and isophthalic acid
CO2H CO2HTiCl489%
CO2HPd/C
H277%
HO2C
CO2H
O2
Co2+/Mn2+
94%
Miller, K. M.; Zhang, P.; Nishizawa-Brennen, Frost, J. W. ACS Sustainable Chem. Eng. 2014, 2, 2053-2056.
Frost, J. W. WO2014144843, March 15, 2013.
Biobased Terephthalic Acid: Scale-Up
CO2H CO2HTiCl4CO2HPd/C
H2
HO2C
CO2H
O2
Co2+/Mn2+
580 g 580 g 400 g 100 g
CO2H90 wt%
3 wt%O
H
CO2H
7 wt%
HO2C
CO2H
99.995 wt%Purified Terephthalic Acid
PTA
Biobased Terephthalic Acid: Next Steps
CO2H CO2H CO2H CO2H
petro petro petro bio bio petro bio bio
Step #1 Step #2 Step #3 Step #4
CO2H
acrylicacid
isoprene
O
OHOH
OHOH
HO
a
a'
(a,a') microbial biocatalysis
3 CH4
3 H2O
9 H2
3 CO6 H2
3 CH3OH1.5 O2
H2O3 H2Ob c d e
(b) steam reforming (c) MeOH synthesis(d) MTO catalysis (e) catalytic oxidation (f) Philips Triolefin Process (g) cracking
7 CH4
7 H2H2
b,c,d f g
• 95% probability of 9.5-13 billion people by 2100.
• Annually, the U.S. will turn 5 billion bushels of corn into ethanol, which is enough food to feed 412 million people for an entire year.
Biobased Terephthalic Acid: Glucose
• In 2013, the U.S. produced 0.69 x 1012 m3 of methane.• In 2013, the U.S. consumed 0.72 x1012 m3 of methane. • In 2014, the U.S. had 10 x 1012 m3 of proven methane reserves.• In 2014, the U.S. had 81 x 1012 m3 of estimated methane reserves.• The U.S. has 1,500 x 1012 m3 of estimated methane hydrate reserves. • In 2013, first marine extraction of methane hydrate (Nankai Trough).
• In 2013, U.S. biogas production was 0.012 x 1012 m3 annually.• Near-term, U.S. biogas production could reach 0.060 x 1012 m3 annually.• U.S. chemical industry consumes 0.046 x1012 m3 of methane.• Methane (wt/wt) has a 25-fold greater impact relative to CO2 on climate
change over a 100-year period.
Biobased Terephthalic Acid: Methane
Thermogenic/Biogenic Methane
Renewable Biogas