65 0 504KB
CATALYSIS Theory and Applications
Paul C.J. Kamer, Gadi Rothenberg, Ron Wever University of Amsterdam
Definition of Catalysis and Catalyst A catalyst is a substance that increases the rate of a reaction remaining itself unchanged
A
B
CAT
Importance of Catalysis • increasingly important in synthesis • selectivity in production of fine chemicals • clean processes, high atom economy (bulk processes) • production of high-tech products / materials • mild conditions (low energy consumption) • environmentally friendly Example: methyl metacrylate (MMA) Old process: 2.5 kg waste / kg product O
+ HCN
HO
CN 1. H2SO4
2. CH3OH
COOCH3
New catalytic process: 50 g waste / kg product CO, Methanol catalyst
COOCH3
+ NH4SO4
Catalyst Activation and Regeneration A + catalyst
B + catalyst
a catalytic reaction wherein the catalyst is unchanged
By-product D Reagent C
active catalyst
Substrate A
inactive Product B catalyst catalyst precursor
a catalytic reaction wherein the catalyst is deactivated and needs to be regenerated (re-activated) or requires an incubation time
How Does a Catalyst Work? •Lowering activation energy •Stabilization of a reactive transition state •Bringing reactants together •proximity effect •orientation effect •Enabling otherwise inaccessible reaction paths
Energy profile of a reaction
Example: Lewis Acid Catalyzed Diels-Alder Reaction −
O +
−
δ
δ
AlCl3
δ
O
AlCl3
Frontier orbitals overlap
HOMO of butadiene (Ψ2) LUMO of ethylene (π*)
LUMO of butadiene (Ψ3*) HOMO of ethylene (π)
Secondary overlap stabilizes endo transition state O
fast
O O
O O
O
HOMO O O
O O
O
slow
O O
O
O
LUMO
Frontier orbital interactions for DA reactions energy
LUMO
LUMO
LUMO LUMO
LUMO LUMO
HOMO HOMO
HOMO
HOMO HOMO
HOMO
X
Z
dienophile with a low energy LUMO
dienophile with neither a low energy LUMO nor a high energy HOMO
dienophile with a high energy LUMO
Influence Lewis Acids on endo-selectivity +
H
CO2Me
O H
+ AlCl3
CO2Me
CO2Me
without AlCl3 at 0° with AlCl3 at 0° with AlCl3 at -80°
O
+ H
88% 96% 99%
AlCl3 H
12% 4% 1%
O
H H
Frontier orbital energies and coefficients acrolein LUMO
2.5
O
.51 -.48
-.39
H
O
.59
-.70
-.09
O HOMO -14.5
-.58
H
.37
H
-7
LUMO
.60
-.30 .48
H
.58
H
O
-.54
-.10
acrolein
.65
H
.53
protonated acrolein
-23.5 HOMO
Increased regioselectivity acid catalyzed DA
X
O -.39
X H
.59
HOMO LUMO without catalysis
O -.09
H H
.60
HOMO LUMO with catalysis
Increased endo selectivity acid catalyzed DA
-.48
O
without catalysis
-.7
HO
with catalysis
Catalysts • general acid and base catalysis (ester hydrolysis), • Lewis acids as catalysts (Diels-Alder reactions), • organic catalysts (thiazolium ions in Cannizzarro reactions), • porphyrin complexes (epoxidations, hydroxylations), • enzymatic processes, • co-ordination complexes (polyester condensations), • catalytic antibodies
world market for catalysts: 9 billion USD
Catalysts affect both rate and selectivity Reaction
A+B
uncatalyzed
d[P]/dt = k1[A][B]
catalyzed
d[P]/dt = k2[Cat][A][B]
Atom economy E factor
P
number of atoms ended up in product number of atoms from the reagents
mass units of waste mass units of product
Diels Alder
+ atom economy 100%
Hydroformylation
cat R R H2/CO
CHO
+R
CHO
atom economy 100%
Examples atom economy "Rh" H 2 /CO
100%
CO
H2
R
R
100%
R "Ru"
R +
100%
"Pd" br
-HBR
26/28 (69 mass percent)
E factor
Industry
Production ton/year
waste/product ratio
Oil Bulk Finechemicals Pharmaceuticals
106-108 104-106 102-104 10-103
0.1 100
Homogeneous catalysis
Definition: Catalyst components and substrates of the reaction are in the same phase, most often the liquid phase (some catalytic reactions in the gas phase are also known). Generally homogeneous catalysis refers to the use of organometallic complexes as the catalysts.
Advantages / disadvantages Advantages: - understandable kinetics - reproducibility - relatively mild reaction conditions - high selectivity - easy modification of catalyst properties - efficiency; all molecules are accessible - mechanistic studies are relatively easy to perform (complex identification by IR, NMR, UV etc.) Disadvantages: - water and oxygen sensitivity - separation of catalyst and products often difficult
Development of Transition Metal Catalysts Choice of metal Use of ligands with proper donor atoms Ligand effects on activity and selectivity Steric effects Electronic effects Bite Angle Secondary interactions Substrate-metal Substrate-ligand Medium effects level of sophistication
Rational catalyst design alkene metathesis R1
R2
R1
3
4
R
R
catalyst: LnM
+
+ 4
R2 3
R
R
R R'
alkyne metathesis R2
R1 R4
+
R3
R1
R2
+ 4
R
3
R
catalyst: Mo(CO)6 + HO rate: 2 mol / mol / h Mortreux (1974)
O t-Bu
"designed catalyst": t-Bu
W
O t-Bu
O t-Bu
Cl
rate: 300,000 mol / mol / h Schrock (1984)
Selectivity in nickel catalyzed butadiene reactions n
n
n
''Ni''
Selectivity to desired product steered by choice of ligands
Chemoselectivity
OH O
H2, kat
O OH
H2
Regioselectivity
CHO CO / H2
CHO
Enantioselectivity
COOR' R
H2 + * + NHCOR" [HRh L 2] R
*
COOR' NHCOR"
99 % ee
Diastereoselectivity
R R
*
OH
*
OH
H2
R
*
OH
Heterogeneous catalysis Advantages: - easy separation of catalyst and products - low sensitivity to water and oxygen - high temperature stability - shape selectivity (zeolites) Disadvantages: - kinetics can be complex - often high pressures and temperatures required - catalyst poisoning by sulfur compounds - sintering - heat transfer - surface chemistry; using a few atoms only
Immobilization of transition metal complexes Supported Homogeneous Catalysts - Organic Polymers - Dendrimers - Inorganic Metal Oxides Supported Aqueous Phase Catalysis Two-phase catalysis
- organic solvents (SHOP) - fluorous phase - aqueous phase
Sol-Gel catalysis
disadvantages:
Extraction (acid / base)
- degradation of polymer - leaching of metal - oxidation of anchored ligands
Ultrafiltration
Product shape-selectivity selective diffusion of para-xylene out of the pores of silicalite
Product shape-selectivity computer simulation of para-xylene in a silicalite pore
Dendrimers as support Dendrimer particle that serves as a catalyst support
Catalyst immobilisation on dendrimers Si
Si Si
Si
Si
Si
Si
Si
Si Si
Si
Si
Si
Si
Si
Si
Si
Si
Si
Si Si
Si
Si P
Si
Si
Fe
Si Si
P Si
Si Si Si Si
Si
Si
Si Si
Si Si
Si
Si
Si
Si
Si
Si
Si
Si
Si
Si
Si Si Si
G.E. Oosterom et al. Chem. Commun.1999, 1119
Si
Ph2P Ph2P Ph2P Ph2P Me Si PPh2 Ph2P 2 Me2Si SiMe2 Me2Si SiMe PPh2 2PPh Ph2P PPh2 SiMe2 2 SiMe2 Me Si Si 2 Si Ph2P Si SiMe2 PPh2 Me2 Si Si SiMe2 PPh2 Ph2P Me2 Si Si Me 2SiMe Ph2P 2 PPh SiMe2 2 Si SiMe2 Si Ph2P Si SiMe2 Me2Si Si Ph2P Si Si PPh SiMe2 2 Me2Si Si PPh2 Si Me2Si Si Me Si Ph2P Me2 2 PPh2 Si SiMe2 Si Me2PPh2 Ph2P Me2Si Me2 Si Si Si Ph2P Me2Si Si Si SiMe2 Si PPh2 Me2 PPh2 Me Si Ph2P Ph2PMe2Si 2 PPh2 SiMe 2 PPh2 SiMe2SiMeSiMe 2 Ph2P 2 PPh2 PPh2 PPh2 PPh2
D. de Groot et al. Chem. Commun.2000, 711
Dendritic transition metal catalysts: covalent approach Core functionalization
Periphery functionalization CAT CAT CAT CAT CAT CAT CAT CAT
CAT
CAT CAT CAT CAT CAT CAT CAT
CAT
CAT
CAT
CAT CAT
CAT CAT CAT CAT CAT CAT
• site isolation • micro-environment
CAT CAT CAT CAT CAT
CAT
• multiple active sites • potential cooperativity • easy accessibility
Direct comparison core and periphery functionalized dendrimers Ph2P Ph2P
[Pd]
OAc
PPh2
Me2N
Fe
Ph2P
N
N
N
N
Fe
Me2N
PPh2
SiMe2
Fe
SiMe2
Ph2P
PPh2
Me2N
SiMe2
NMe2 PPh2
Fe Ph2P
90
linear, trans
linear, cis
branched
80
Fe
Si SiMe2
Me2N Ph2P
NMe2 PPh2
Me2 Si
Fe
Si
Si
Si
Si Me2
Ph2P Me2N
70
PPh2
SiMe2
Fe PPh2
Ph2P
Fe
Me2Si
NMe2
Me2Si Si
PPh2
conversion / %
Fe
60
Ph2P Me N 2
50
Me2Si
Fe Ph2P
40
PPh2
Fe
NMe2
NMe2
Ph2P
30
PPh2
PPh2
SiMe3
Me3Si
Me3Si
10
Me3Si
2
4
6
8
reactor volumes
Room temperature, solvent: CH2Cl2, P/Pd=2.
10
SiMe3 SiMe3
Si
Si
SiMe3
Si
Si
Si
Si
SiMe3 SiMe3
Me3Si
0
SiMe3
SiMe3 Me3Si
Me3Si
0
SiMe3
Me3Si
NMe2
Fe
Ph2P
20
PPh2
Me2Si
Me2Si
Si P
Si Me3Si
SiMe3
Fe P
Me3Si
Si
Si Me3Si
Si
Me3Si Me3Si
Si
Me3Si Me3Si Me3Si
SiMe3 SiMe3
Si
Si SiMe3
Si
Si SiMe3 3 SiMeSiMe 3
Me3Si
SiMe3 Me3SiMe3Si
SiMe3
Biocatalysis: the use of enzymes or cells Enzyme optimization: • protein “engineering” • molecular evolution • enzyme “engineering” Enzymes can be applied in: • Water • Organic solvents • Supercritical CO2 • Ionic liquids
Energy profile of an enzyme catalyzed reaction
Enzymes give great rate enhancements Michaelis-Menten parameters for selected enzymes
Enzyme specificity
Examples of classes of enzymes
Coenzymes, vitamins and metals Some important coenzymes and related vitamins
Active site of carboxypeptidase A
Ideal catalyst characteristics
• • • •
High activity (mild reaction conditions) High selectivity (chemo, regio, enantio) Stable catalyst Easy separation and reuse of catalyst
New “green” processes:
• Atom economic • No or as little as possible waste • decrease in solvent use • Mild reaction conditions • Catalytic use of reagents instead of stochiometrisch • Non-toxic reagents, • New sustainable starting materials