the petrochemical industry: a 20 century success story€¦ · carrier gas (n. 2) inject catalyst....
TRANSCRIPT
The Petrochemical Industry: A 20th Century Success Story
fuel
InterestingMaterials
Catalysis Enabling 21st Century E2
Catalysis
Energy
Environment
Reactions of chlorine oxyanions Biomass conversion Kinetics of olefin polymerization
Perchlorate: Rocket Science
Cl OO
O-
O
Interferes with the functioning of the thyroid.
Rocket fuel, missiles, and fireworks.
Water Contaminant
Uses Toxicity
Peter Waldman, The Wall Street Journal- Online (WSJ.com), December 16, 2002.
Reduction Via Oxygen Atom Transfer (OAT)
O
NOReO
ON
O
Solv
O
ClO
OO R
SR4 Cl- R
SR4
O
O
NOReO
ON
O
OH2
O
ClO
OO
RS
RR
SR
O
ReO OO
N NOO
O
O
ClO O
f ast
rds
Abu-Omar, Chem. Comm. 2003, 2102.Abu-Omar et al Inorg. Chem. 2004, 43, 4036.
Mechanism
John Shapley (UICU)
Environ. Sci. Tech. 2007, 41, 2044.
Perchlorate-Reducing Bacteria (PRB)
Coates et al, Nature Reviews Microbiology 2005, 2, 596.
1-1000 per g soil or water
Fe
Chlorite Dismutase
Cl- + O2
ClO2-ClO4
-
ClO2-
Fe
Perchlorate Reductase
Pcr B Pcr A
Pcr DPcr C
Cytoplasm
Periplasm
Organic carbon
CO2 + H2O
ClO3-
e -
Chlorite Dismutase
ClO2- O2 + Cl -
• Homotetramer, 100 -120 kDa• 1 heme b per monomer• Histidine ligated heme • No sequence homology with other proteins• Km ~ 215 µM• kcat ~ 7500 s-1
• kcat/Km = 3.5 x 107 M-1s-1
N
NN
N
COOHHOOC
FeFeIII
ClO2-
Cl-
ClO3-
HPO42- Compound Ci
mM
C∞ Recovery % Yield
O2 0 4.6 mL 4.6 mL 41
Cl- 2.8 25.7 mM 22.9 mM 49
ClO3- 1.6 1.4 mM 0 0
ClO2- 46.7 26.4 mM 26.4 mM 51
ClO2- cld O2 + Cl-
85 nM
0.050 M
MikeAmanda
19th Century mass spectrometry
MASS ANALYSER
Stirred not shaken
Carrier gas(N2)
Inject catalyst
Isotope Labeling
ClO2- Cld
H218O
O2 + Cl-
16O2
N2H2ON
H2
No incorporation of 18O from H2
18O into O2 product
log
inte
nsity
Both O atoms in the evolved O2derive from chlorite
Cl18O2- Cld
H2O O2 + Cl-
77%
ClO2_enriched_18O_2 #115-139 RT: 0.68-0.83 AV: 25 NL: 2.39E2T: ITMS - p ESI Full ms [50.00-100.00]
50 55 60 65 70 75 80 85 90 95 100m/z
0
5
10
15
20
25
30
35
40
45
50
55
60
65
70
75
80
85
90
95
100
Rel
ativ
e A
bund
ance
71
93
69
95
7353
9985
5589 9779
816751
8775 9177
Cl18O2-
Cross Over Experiment
O2
OO
O2
Freeze-Quench EPR
FeIII
NHis
(OH2)
heme bClO2
-
HN
NNH
N
COOHHOOC
FeIV
NHis
O
heme b FeIV
NHis
O
heme b
TrpH
a
b
c
b-c
Sim.
Mechanistic Insight
FeIII
NHis
ClO2-
FeIV
NHis
O
O Cl
FeIII
NHis
OO Cl
Cl- + O2
kr ~ 107 s-1
OH2
FeIII
NHis
O OCl
FeIV
NHis
O
Trp189k2 = 170 s-1
Deactivation
Proc. Natl. Acad. Sci. USA 2008, 105, 15654–15659.
Structural Confirmation
Daniël C. de Geus et al J. Mol. Biol. 2009, 387, 192-206.
• “The heme active-site pocket is solvent accessible both from the inside and the outside of the ring. Moreover, a second anion binding site that could accommodate the assumed reaction intermediate ClO‾ for further transformation has been identified near the active site.The current crystal structure confirms and complements a recently proposed catalytic mechanism that proceeds via a ferryl species and a ClO‾ anion.”
•Azospira oryzae Cld
Density Functional Theory
With Derat, Submitted for publication.
QM/MMB3LYP
ClO2-
Fe(Por)1 mol%pH = 7.1H2O
O2 + Cl- + ClO3-
First Generation Cld Model Complexes
N
NN
N
Ar
Ar
ArAr Fe
[Fe(TF4TMAP)]5+[OTf-]5
[Na+]3[Fe(TPPS)]3-
[Fe(TMAP)]5+[Cl-]5 NMe3
NMe3
F F
FF
SO3
Ar =
Ar =
Ar =
20 – 30%
Catalysis via Two Pathways
Angew. Chem. Int. Ed. 2008, 47, 7697-7700.Inorg. Chem. 2009, 48, 2260-68.
Mn versus Fe pH = 5.0
TOF = 670 h-1
ClO2-
Cl-
ClO3-
Scott
ClO2 gas even at pH 7
Mechanism
Angew. Chem. Int. Ed. 2011, 50, 699.
Groves Angew. Chem. Int. Ed. 2011, 50, 695.
Global Energy Consumption
0
5
10
15
20
25
30
35
40
Oil Coal Gas Nuclear HydroRenew
% G
loba
l prim
ary
ener
gy c
onsu
mpt
ion
BP Energy Year in Review
Planes, Trains, & Automobiles
US Oil Imports in 2009
Country/Region Million tons Percent (%)
South America 119 19
Middle East 120 19Canada 122 20
Mexico 65 11Norway 43 7Africa 124 20Old Russia 24 4Total 617 100
But Where is the Proven Oil Reserves
Proven Oil Reserves
Country Reserves (109 bbl)
Saudi Arabia 260Canada 179Iraq 115Iran 105Kuwait 99UAE 97Venezuela 80Russia 60Libya 42Nigeria 36U.S. 21
5 out of the top 6 countries are in the Middle East.
The agronomic footprint of biofuel feedstock to displace 30% gasoline by 2030 with ethanol
Biological conversion of biomass to biofuel
Phenylpropanoid metabolism is critical for plant survival
http://givingspace.org/benlomond/up%20redwoods.jpg
Hatfield and Vermerris Plant Physiol. 2001, 126, 1351-1357.
• UV resistance• structural support• water transport
wild type
ref3-1
Catalytic Conversion Processes
Apply and optimize catalytic transformations to a range of biomass components and genetic variants.
Biomass
HydrocarbonLiquid Fuels
f ast hydropyrolysis polysaccharides
lignin componentsfururals
biomass-derived compounds
High-ValueOrganics
Controlling reaction selectivity towards hydrolysis and dehydration vs degradation critical to biofuel production
Leaving lignin unmodified
O
R
OH
OH OO
R
OH
HO O
n
R: -CH2OH Cellulose
R: -OH Hemicellulose
HydrolysisO
H
HO
H
HO
H
H
OHH
R
OH
Degradation
O
O
H
R
R: -CH2OH
R: -H
HMF
FurfuralR: -CH2OH
R: -OH
Glucose
XyloseR: - CH2OH CelluloseR: - OH Hemicellulose
R: - CH2OH GlucoseR: - OH Xylose
R: - CH2OH HMFR: - H Furfural
Hydrolysis Dehydration
Simple Sugars AldehydesCellulosic Biomass
H+ H+
The Acid Route Dilemma
Unusable “Tar”
Degradation
Selective Hydrolysis and Conversion
OOH
OHO
OHO
HO OH
OH
170 °C, 10 min+
Biomass Lignin & CelluloseXylose
filterAcid catalyst~200 °C, 4 min
OO
With Prof. Nate Mosier
furfural> 80% yield
Eurick & Shuo
> 90% yield
Pd/C~ 10 min
Me-THF
O
Biomass variants
Biomass Glucan
(Cellulose)
Xylan
(Hemi-cellulose)
Other Structural Carbo-hydrates
Lignin Extractives Other
(Ash, protein, etc.)
Switchgrass 35% 21% 3% 20% 10% 11%
Lodgepole Pine 25% 18% 2% 28% 12% 15%
Hybrid Poplar 45% 18% 4% 21% 8% 4%
One-pot furfural from biomass
Sample Reagent/ Catalyst T (@ 200 °C)/ min
Xylose % conversion
% Yield furfural
Pure xylose (10 g/L)
ZnCl2
Maleic acid
Maleic acid + ZnCl2
H2SO4
10
10
10
5
100
100
100
100
50
90
90
65
Switchgrass Maleic acid
Maleic acid + ZnCl2
H2SO4
10
10
5
100
100
100
85
80
55
Poplar Maleic acid
Maleic acid + ZnCl2
H2SO4
10
10
5
55
100
100
93
85
57
Pine Maleic acid + ZnCl2
H2SO4
10
5
100
97
53
34
Tandem hydrogenation of acetal products from Ff
Ether hydrocarbon products including isomers
GC1H NMR
Cyclic ethers
O O
HOH
OHHO O
O
O
O
O
O
O
O
OHOH
OH OH
O O
OO
Lewis Acid Cat.neat, 100 oC
Pd/CH2 (500 psi)room temp.
O
OO
OO O
Lignin Structure
O
O OH
OH
O
O
O
OH
OH
OH
OO
OH
HO
OH
O
O
OOH
OHO
O
OH
O
OH
O
OH
OH
O
OH
O
O
OH
OO
OH
OH
O
OH
OH
OH
Hardwood lignin
Sinapyl alcohol conifryl alcohol p-coumaryl alcohol
• UV resistance• structural support• water transport
0
200
400
600
800
1000
1200
1400
4 8 12 16 20
pA
Time (min)
Vanillyl Alcohol (a lignin monomer model)
OH
O
OH
O
O
OH
~63%
~23%
~7%
~7%
Trenton
HO
OOH
1 mol% MTO/Pd/C300 psi H2, 150 oC
THF, 2 h
0
500
1000
1500
2000
4 8 12 16 20
pA
Time (min)
Preserving the aromatic group!
OH
O
BHT
>99%
HO
OOH
1 mol% Zn/Pd/C300 psi H2, 150 oC
THF, 2 h
0 5 10 15 20 25
pA
time (s)
Lignin dimer
BHT
OH
O
OH
O
OH
O
OH
O
O
HO
1 mol% Zn/Pd/C300 psi H2, 150 oC
THF, 2 hlignin dimer
MS of oak lignin
400 800 1200 1600 2000
inte
nsity
m/z
With Profs. Joe Bozell and Hilkka Kenttämaa
Degradation of oak lignin
400 800 1200 1600 2000
inte
nsity
m/z
195
297
427
1 mol% Zn/Pd/C300 psi H2, 200 oC
THF, 2 hOak lignin
Degradation of oak lignin
0
20
40
60
80
100
400 800 1200 1600 2000
rela
tive
inte
nsity
m/z
195
297
427
Tailored biomass
With Clint Chapple
Acknowledgments Postdocs
Dr. Michael Zdilla Dr. Trenton Parsell
Graduate Students Dr. Amanda Lee Dr. Jennifer Petersen Scott Hicks Dr. Jeanette Zeigler Andrew Evans Ben Wegenhart Shuo Liu
Collaborators Jennifer DuBois (Cld, Notre Dame) Etienne Derat (DFT, Paris VI) Hilkka Kenttämaa (MS on lignin,
Purdue) Joe Bozell (Lignin samples, UT) Clint Chapple (Engineered biomass,
Purdue) $upport
The National Science Foundation (ClO2
- chemistry) DOE-BES-EFRC (Biomass
conversion)