Title: Martyn Poliakoff
1Catalyddion Aml-Ochrog mewn Hylyfoedd Uwchradd
- Martyn Poliakoff
- martyn.poliakoff_at_nottingham.ac.uk
2Supercritical Fluids
- Gases e.g. CO2, C2H4, H2O compressed until they
are nearly as dense as liquids - SCFs can dissolve solids solubility increases
with density (applied pressure)
3Critical Points
Pc
4Supercritical Catalysis
- Catalysis in scCO2- Hydrogenation,
Hydroformylation - Supercritical Water
- Biocatalysis
5Miscibility of H2/scCO2
Higher Concentration of Dissolved H2 in scCO2
Howdle, S. M., Healy, M. A., Poliakoff, M. J.
Am. Chem. Soc. 1990 112, 4804. Jessop, Ph. G.,
Ikariya, T., Noyori, R. Nature 1994, 368, 231.
6Continuous Supercritical Hydrogenation
7Other Hydrogenations successfullycarried out in
scCO2 and scPropane
8scCO2 Chemical Plant opened July,2002
- continuous
- multipurpose
- 1000 ton p.a.
Thomas Swan Co
9Hydrogenation of Isophorone
The product by-products have similar boiling
points Conventional process requires an
expensive downstream separation
scCO2 - quantitative, no by-products
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12scCO2 and Ionic Liquids
scCO2 very soluble in ILs ( 0.6 mole
fraction) ILs are insoluble in scCO2 L.A.
Blanchard, D. Hancu, E.J. Beckman and J.F.
Brennecke, Nature, 1999, 399, 28 scCO2 can
extract many organics from ILs L. A. Blanchard
and J. F. Brennecke, Ind. Eng. Chem. Res., 2001,
40, 287
13Bi-phasic Catalysis Cole-Hamilton
P. B. Webb, M. F. Sellin, et al. J. Am. Chem.
Soc.,2003, 125, 15577
14Green Chemistry 12 Principles
P R O D U C T I V E L Y
- Prevent wastes - Renewable materials - Omit
derivatization steps - Degradable chemical
products - Use safe synthetic methods -
Catalytic reagents - Temperature, Pressure
ambient - In-Process Monitoring - Very few
auxiliary substances - E-factor, maximize feed in
product - Low toxicity of chemical products - Yes
its safe
- Prevent wastes - Renewable materials - Omit
derivatization steps - Degradable chemical
products - Use safe synthetic methods -
Catalytic reagents - Temperature, Pressure
ambient - In-Process Monitoring - Very few
auxiliary substances - E-factor, maximize feed in
product - Low toxicity of chemical products - Yes
its safe
15Gas-Expanded Liquids
Increasing Pressure
16 Hydrogenation of a-pinene A. Serbanovic, V.
Najdanovic-Visak, A. Paiva, G. Brunner, M.
Nunes da Ponte 8th ISSF, Kyoto
17Gas-Expanded liquids (GExLs)
- 1. Autoxidation by O2 in GExLs,
- DH Busch, B Subramaniam co-workers, Green
Chem., 2004, 6, 387. - 2. Enhanced Solubility of gases in GExLs,
- JF Brennecke coworkers, Ind. Eng. Chem. Res.,
2006, 45, 5351. - CO2-Protected Amine Formation in GExLs
- X. Xie, C. L. Liotta C. A. Eckert, Ind. Eng.
Chem. Res., 2004, 43, 7907.
18Hydrogenation of Isophorone
Reaction has a high space-time yield How is this
influenced by the phase behaviour of the system?
19Isophorone /CO2/H2 phase boundaries
M. Sokolova Ke Jie
20CO2- expansion Hydrogenation
- Increases solubility of H2
- (B. Subramaniam, J. Brennecke)
- Increases diffusion ? faster transport across
phase boundary (EJ Beckman) - Reduces viscosity
- All of these accelerate reaction
21Hydrogenation of sertraline imine in CO2expanded
THF
22Commercial Route to Zoloft
23Continuous hydrogenation of rac-sertraline in
scCO2/THF
- Investigate both chemoselectivity
diastereoselectivity - Aims (1) lt 1.5 dechlorination
- (2) gt 928 de
P. Clark
24Hydrogenation of rac-sertraline imine in scCO2/THF
Catalyst de () from NMR de () from NMR
Catalyst cis- trans-
5 Pt/ C 56 44
2 Pd/ C 87 13
5 Pd/ CaCO3 97 3
- System pressure (125-175 bar) has little effect
on selectivity
(Conditions 175 bar 3x excess H2 0.4 ml/ min
org flow 0.1 M soln in THF 0.5 g catalyst 1.0
ml/ min CO2 flow)
25Summary
- Switch from Batch to Continuous
- Dechlorination is reduced in scCO2 why?
- One of the first examples of diastereoselective
hydrogenation in scCO2 - First example of hydrogenation of final stage
pharmaceutical in scCO2
26Supercritical Catalysis
- Catalysis in scCO2
- Supercritical Water- Selective
Oxidation, Formation of Caprolactam - Biocatalysis
27Total Oxidation in scH2O
- Tc 374 oC pc 218 atm.
- At 300 oC, H2O is similar to acetone
- O2 is miscible with H2O above Tc
- Already in commercial use
28Johnson Matthey ChematurAquaCatProcess for
Catalyst Recoveryopened Oct 10th 2003
29Heterogeneous Catalyst Recovery
Before
After
30Partial oxidation in scH2O?
Nottingham P.A. Hamley, E.G. Verdugo, J.
Fraga-Dubreuil, C. Yan, E. Venardou, R. Auerbach,
R.J. Pulham,T. Ilkenhans, M.J. Clarke, J.M.
Webster, M. Thomas, A. Johal. INVISTA Performance
Technologies, UK W.B. Thomas, G.R. Aird, I.
Pearson, S.D. Housley, A.S. Coote, K. Whiston,
L.M. Dudd, J. Fraga-Dubreuil (ICI D.A. Graham, P.
Saxton)
31Oxidation of p-Xylene
- 0.7 Mton p.a. per plant
- TA insoluble in CH3COOH
- 18 of world production of CH3COOH lost in the
process
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33TA
34Oxidation of p-Xylene / scH2O
PA Hamley, et al. Green Chem. (2002) 4, 235
(2005) 7, 294
35Oxidation of p-Xylene in scH2O
36Selective Oxidation in scH2O
- If our results are scalable,
- total elimination of CH3COOH
- increased energy recovery compared to existing
process - significant reduction in cost of manufacturing TA
37EXAFS Molecular Dynamics Results with 0.4 m
MnBr2
W. Partenheimer, Y. Chen, J. L. Fulton J. Am.
Chem. Soc. 127, 14086, (2005)
38IR spectroscopy in scH2O
First achieved 1967 (Franck Roth)
Much work by T. B. Brill et al. J. Phys.
Chem. (1996) 100, 7455
Recent work by Y. Ikushima et al., Achema,
(2003)
39FTIR of Water
6.62
25 µm pathlength
6.0
5.5
5.0
4.5
4.0
A
3.5
3.0
2.5
2.0
1.5
1.0
0.5
3600
3200
2800
2400
2000
1800
1600
1400
1200.0
4000.0
cm-1
40High T P IR Cell Yu. E. Gorbaty
41Hydrolysis of MeCN
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43Raman Spectroscopy
Eleni Venardou Appl. Spectrosc., (2003) 57
44Raman Spectra of CH3CN in ncH2O
no added acid 300 C, 300 bar
45Raman Spectra of CH3CN in ncH2O
46Hydrolysis of MeCN Effect of Concentration
47Caprolactam
- Industrial synthetic route
- Problem
- 5 kg (NH4)2SO4 are made per kg CPL
48Alternative Synthesis
- Cheaper feedstock,
- No cyclohexane oxidation
- No ammonium sulphate
Yan Chong
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50Strategy
H. Vogel et al. Chem. Eng. Technol. (1999) 22,
494 70 conv. ACN but only 45 yield CPL 400
oC, 4 min. residence time
- Study effects of T and p
- Concentration of feedstock
51Caprolactam Summary
- Single-step green process
Hydrolysis, SCW
Cyclization, SCW
6-Aminocapronitrile, ACN
6-Aminocaproic acid amide, ACA
CPL
- gt60 yield of CPL within lt2 min
- No organic solvent
- No additional catalysts
C. Yan et al. WO2006078403
52Supercritical Catalysis
- Catalysis in scCO2
- Supercritical Water
- Multiphasic Biocatalysis
- Helen Hobbs, Neil Thomas
53Enzymes in Fluorous Biphase
PFMC Perfluoro- Methyl Cyclohexane
54How can one dissolve an enzyme in a fluorous
solvent (or even scCO2)?
55Hydrophobic Ion Pairing
56Fluorinated Anionic Surfactant
Krytox NH4 n 14/2500 KDP NH4 n 7/1400
Soluble in Fluorous phase and scCO2
57Cytochrome c inaqueous buffer
58Fluorous Phase added
Fluorous Krytox
59HIP extraction into theFluorous Phase
Butis the enzyme really dissolved?
60Dynamic Light Scattering Candida rugosa lipase
Expected Diameter 6.8 nm
61KDP surfactant mw1400 Expected length 1.4 nm
62Expected diameter 9.6 nm (CRL-KDP)
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64Biocatalysis in Fluorous Biphase
65CMT-KDP Recycling (FBS)
66Dissolving Biomolecules
- Precipitation from aqueous buffer
Dissolve in scCO2
67Biological Molecules in scCO2
Cytochrome C
68Supercritical Catalysis
- Continuous Reactions
- Key aspect of supercritical fluids
- New Developments Green technologies are not in
competition - Partnership between Chemists Chemical Engineers
69DICE Driving Innovation in Chemistry Chemical
Engineering
- EPSRC initiative led by Nottingham to stimulate
research at the interface of Chemistry/Chem.Eng - 6 new faculty posts in Chem. Chem. Eng.
including 3 joint posts - Big opportunities for collaboration particularly
with POC at Cardiff
70P Licence NR Thomas PA Hamley
All our Students, Postdocs and Collaborators
P. Fields, R. Wilson, M. Guyler
INVISTA, Thomas Swan Co, GSK, ICI EPRSC, Royal
Society, EU Marie Curie
71- Impact
- Factor
- 3.26
- www.rsc.org/
- Greenchem
martyn.poliakoff_at_ nottingham.ac.uk
72GSC-33rd International Conference on Green
Sustainable Chemistry
1-5 July 2007, Delft, The Netherlands
73GSC-33rd International Conference on Green
Sustainable Chemistry
Professor Graham Hutchings RSC Green Chemistry
Lecturer
1-5 July 2007, Delft, The Netherlands