E2C 2013 Budapest Y Jiang R Kunjanpillai S Chakraborty F Zhou O Blacque T Fox and H Berke Strategies for Homogeneous Carbon Dioxide Hydrogenations Search for ID: 479520
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Slide1
A Diversity of Chemical Strategies to Implement Homogeneous Carbon Dioxide Hydrogenations
E2C 2013, Budapest
Y. Jiang, R.
Kunjanpillai
, S.
Chakraborty
,
F
. Zhou
O.
Blacque
, T. Fox and H.
BerkeSlide2
Strategies for Homogeneous
Carbon Dioxide Hydrogenations
Search
for
molecular middle transition element catalystsCheap catalysts and processesProcesses running at ambient or near ambient conditionsOxygenates (CnHmOo) as productsUse of molecular hydrogen from ’renewable’, ‘waste’ or CO2-free sources
‘Non-noble Metals for Noble Tasks’
As for methanol as the simplest oxygenate productCO2 + 3H2 CH3OH + H2O
Homogen.cat
MeOH available since the 1920s by heterogenous CO hydrogenationPotential energy carrierSmall scale and de-centralized production seems possibleFacile convertion to other oxygenates ( for instance DME) or hydrocarbonsToxicLow boiling point
Pros
ConsSlide3
Middle
Transition Elements
in
Homogeneous
Hydrogenation Catalysis Middle transition elements particularly rhenium
is bordering precious metals may
have retained some of the „noble“
properties,
like high affinity to hydrogen and to unsaturated organic molecules-
Isoelectronic
replacements
in precious
metal
complexes
may
generate active catalysts; for instance the Ru-L unit (L= 2e- donor) replaced by the Re-NO unit Middle transition element seek stable 18e- configurations; disadvantage for catalysis, which needs permanently or temporarily vacant coordination sites Tuning of the ligand sphere is required to stabilize vacant sites via ligand effects, such as of ligands with variable electron counts, large-bite-angle-effects of bidentates, large cone angles of monodentates, cis labilization effect and the trans influence/effect and othersSlide4
Pd
125
200
275
350
Electrochemical
Volcano Plot for Hydrogen
1051M-H bond strength (kJ/mol)ThermodynamicsKineticsHydrogen evolution
reaction log(i0) (A/cm
-2)S. Trasatti, J. Electroanal. Chem. 39 (1977) 163S. Trasatti, Electrochim. Acta 39 (1994) 1739Which metals are preferred in hydrogen catalysis?Slide5
Stages
of
CO2
Reduction
by H2Carbon oxidation state from +IV to -II
Formic acid or formate stage(thermodynamically
unstable, but kinetically too stableHydroxy carbene or formaldehyde stage(joint catalytic processes to make ‘formoses’ (CnH2nO
n) seem possible)
Carbonic acid, CO2 or carbonate stageMethanol stage, potential to be converted into other oxygenates Formation of esters via the reaction of carbonic and formic acid and derivatives with alcohols including
the product methanol (
catalyzed by protons) may
help to overcome the reactivity deficit
of
formic
acid and derivatives. Esters are more easily reduced than acids or their anions Slide6
Hydrogenation
of CO
2
to Formic Acid and Formates
hydridic
protonicAs a polar molecule HCOOH would be prone for reactions with heterolysis of
H2!
Thermodynamics of the hydrogenation CO2 to formic acid:Additional driving force by salt formation
!Despite
their thermodynamic
instability, formic
acid
or
formate
salts are kinetically (too) stable!pKa = 3.8CO2(g) + H2(g) → HCOOH(l) ∆Go = 32.9 kJ/mol; ∆Ho = -31.2 kJ/mol; ∆So = -215 J/(mol K) CO2(g) + H2(g) + NH3 (aq) → HCOO- (aq) + NH4+(aq) ∆Go = -9.5 kJ/mol; ∆Ho = -84.3 kJ/mol; ∆So = -250 J/(mol K)CO2(aq) + H2(aq) + NH3 (aq) → H(CO)O- (aq) + NH4+(aq) ∆Go = -35.4 kJ/mol; ∆Ho = -59.8 kJ/mol; ∆So = -81 J/(mol K)Slide7
Cat/ (
mol
%)
Substrate
Co-catalyst
BCF = B(C6F5)3
Temp(°C)H2
(bar)Time(h)TOF(h
-1)
Conv(%)Mo/0.051-hexene -14060
0.5
912
21
Mo/0.03
1-hexene
Et
3
SiH/BCF
140602525375W/0.0201-hexene Et3SiH/BCF140600.5820080Mo/0.081-octene Et3SiH/BCF14060<2350075W/0.0491-octene Et3SiH/BCF140600.5361588Mo/0.01Styrene Et3SiH/BCF140602207984W/0.037Styrene Et3SiH/BCF140600.5
2064
39
Mo/0.03
1,7-octadiene
Et
3
SiH/BCF
140
60
2
1056
65
Mo/0.07
Cyclohexene
Et
3
SiH/BCF
140
60
<10
200
100
Mo/0.07
Cyclooctene
Et
3
SiH/BCF
140
60
3
1355
55
Mo/0.07
α-methyl styrene
Et
3
SiH/BCF
140
60
16
205
60
Mo/0.09
1,5 cyclooctadiene
Et
3
SiH/BCF
140
60
14
200
74
c
at: M = Mo,W
Olefin Hydrogenations with Mo and W Nitrosyl Hydride Catalysts
S.
Chakraborty
, T. Fox, O.
Blacque
, 2013
submittedSlide8
Hydrogenation
of
CO
2
to Formic Acid Using a Tungsten ComplexBase = DBUSlide9
Large
cone
-angle „
on - off“
chelate
phosphine! Exploitation of Ligand
Effects to Make the Hydrogenation of CO2
with a Tungsten Hydride Catalytic
Carbynes
like nitrosyls (3e donors!) are trans influence and trans
effect
ligands
and activate
trans
positions
.
Tungsten has great affinity to H2!Slide10
Catalytic
CO
2
Hydrogenation
to FormateProducts [HCOO][DBUH] and HCOOH•DBU precipitate from
toluene solutionLow energy ‘Organo-catalytic
’ transition state
catSlide11
Rhenium
Based
Catalytic CO
2
Hydrogenation to Formate and MethanolSlide12
FLP Type
Activation
of
CO
2 with Rhenium
Complexes and a Lewis AcidSlide13
FLP Type
Activation
of
CO
2 with a Rhenium Hydride and B(C6F5)3
as Lewis Acid – Stoichiometric ReactionsFrustrated
Lewis pair (FLP) where the hydride plays the role of a Lewis base!Fully
characterized
by NMR in solutionCrystal structureJiang, Y.; Blacque, O.; Fox, T.; Berke, H., J. Am. Chem. Soc. 2013, 135, 7751-7760Slide14
A Stable
Formate
Dihydrogen
Complex and Subsequent Stoichiometric Reaction with Et3SiHIsolated and fully characterized
Jiang, Y.; Blacque, O.; Fox, T.; Berke, H., J. Am. Chem. Soc. 2013, 135, 7751-7760Slide15
Catalytic Reduction of CO
2
with Et3SiH
H
2
CH
2
OHOMeH2OHydrogenationHydrosilylationSlide16
Hydrogenation
of
CO2
with
a Rhenium Hydride/Lewis
Acid System in Presence of TMPStructure of [TMPH][HCOO]Slide17
Proposed Mechanism for the Rhenium Catalyzed
CO
2
Hydrogenation In Presence of B(C
6
F5)3 and TMPSlide18
Hydrogenations
with
Rhenium
Nitrosyl
Complexes Bearing Large Bite-Angle Xantphos Diphosphines
Trans NO
reactive siteKinetic ‘isomer’?
Cis NO
reactive siteThermodynamic isomer?Xantphos framework may ‘bite’ bi- or tridentate
Reactive
site
interconversion
Ammonia
complex
(NO/Br disorder)Slide19
Rhenium
Based Catalytic
CO
2
Hydrosilylation and Combined Hydrogenation/Hydrosilylation to Methanol and Derivatives
Hydrogenation/
hydrosilylation with TONs up to 330:
Hydrosilylation
with TONs up to 410:
1
2Slide20
Rhenium
Based
Catalytic CO2
Combined
Hydrogenation/Hydrosilylation to Formate DerivativesSlide21
Substrate
Catalyst (
mol
%)
Co-catalyst
SolventProductTONYield (%)
0.02 n-Bu
4NBr THF PhCH
2OH
500 100 Benzaldehyde0.02
-
Toluene
PhCH2
OH
4807
96
Acetophenone 0.05-Toluene PhCH(OH)Me2000> 99 0.5 -THF CH3OH 112 56 0.5 n-Bu4NBr EtOH CH3OH 161 81 0.2-MeOHHCOONa285.6 0.2-D2O/THFHCOONa6813.6
0.5
n-Bu
4
NBr
EtOH
CH
3
OH
H(CO)ONa
20
24
10
12
Rhenium
Based
Ester, Aldehyde, Ketone
and
Bicarbonate
Hydrogenation
to
Alcohols
140 °C, 60 bar H
2Slide22
Co-catalyst 1 /Equiv.
Co-catalyst 2 /Equiv
./acid
CO
2
/H2 (bar)TON--10/30
07n-Bu4NBr /5
-10/3028n-Bu4NBr /5
-
10/3026c--10/3013n-Bu4NI /100
-
10/30
11
NaI/100
-
10/30
05
n
-Bu4NBr /2-10/3020n-Bu4NBr /50-10/3030n-Bu4NBr /100-10/3030Et4NBr /100-10/301.6n-Bu4NBr /5-10/300.9-EtOH/25010/3006n-Bu4NBr /100EtOH/25010/3033n-Bu4NBr /5EtOH/100/p-TsOH10/3029gn-Bu4NBr /5-20/6088Rhenium Based and Halide Co-catalytic CO2 Hydrogenation to Methanol
Optimum
loading
of
co-cat.bromide
Improved
performance
by
EtOH
add
.
No
improvement
by
acid
add
.
H
2
pressure
matters
Is
formate
ester
formation
crucial
to
catalysis
?
What
is
the
influence of the produced water on ester formation?Slide23
Rhenium
Based
Hydrogenation of
Methyl
Formate to MethanolMethyl formate cycleFormaldehyde
cycleSlide24
Remaining
Questions
on
the CO2 Hydrogenation to MethanolRelevance of formic ester formation Can ester formation
be enhanced by protic additives?Role of the water product for the ester formation. Removal of
water required?Change type of the hydrogenation course and develop two-step hydrogenation processes? CO2 Formic acid
formic acid
ester methanol CO2 carbonic acid carbonic acid diester methanol catalysts optimizationsSlide25
Acknowledgements
Preparative
work
Y
. Jiang,
R. Kunjanpillai, S. Chakraborty, F. ZhouX-ray structures and DFTO. Blacque NMRT. Fox
Financial SupportFunds of the University of
ZurichSwiss National Science FoundationLanxess AG, Leverkusen, GermanySlide26
Utilization
of
Metal-Ligand
Activation
of CO2Slide27Slide28
Stoichiometric
CO
2
Hydrogenation
to FormateSlide29
Cat
Base
Time (h)
Yield (%)
Mo
Na[N(SiMe3)2]154
WNa[N(SiMe3)2]
152
Catalytic
CO2 Hydrogenation to FormatePoor catalysis due to a too
stable
CO
2 complex!Slide30
Rhenium
Based
Catalytic CO2
Hydrogenation
/Hydrosilylation to Methanol and Silyl DerivativesSlide31
Reaction
Center
Mediated
Splitting
Pathways of DihydrogenMononuclear and dinuclear dihydrogen complexes prepare the H2 molecule for the splitting reaction by polarization Slide32
Single-step processes combined splitting and H-transfers (rare)Multi-step processes
separate splitting and H-tranfersActivation
of H2 = H2 splitting and H-transfers
Splitting
Homolytic splitting H
2 2 H Wilkinson/Osborn-type hydrogenation catalyses with oxidative addition of H2Heterolytic splitting H2 H- + H+ Ionic hydrogenations (protonic-hydridic reactivity, bifunctional activation). Usually achieved by deprotonation of H2 complexes with a baseH-TransfersSimultaneous (concerted
) polar transfers of polarized H atoms (H(+) protic and H(-) hydridic)Stepwise transfers: homopolar H atom transfer
via insertion into the M-H bond and reductive eliminationHeteropolar stepwise transfersH H
H2
Substrate XYHXYHPrinciples of H2 reactivityHomolytic, heterolytic splitting?
H-transfers: homopolar, heteropolar?
Sequence
of
Transfers?
Principles
of Hydrogen ReactionsH. Berke, ChemPhysChem, (2010), 11, 1837Slide33
Interconversion
of
‘
Isomeric
’ Xantphos Nitrosyl Rhenium Complexes via Anionic Trihalo Intermediates – Basis
for the Catalytic Halide Effect
I(trans) more reactive than I(cis)!Slide34
Cis P
iPr
3 ligands: P(1)-Re(1)-P(2), 103.78(2)
Structure
of 3a