Martyn Poliakoff - PowerPoint PPT Presentation

1 / 73
About This Presentation
Title:

Martyn Poliakoff

Description:

Hylyfoedd Uwchradd Martyn Poliakoff martyn.poliakoff_at_nottingham.ac.uk Critical Points Miscibility of H2/scCO2 Continuous Supercritical Hydrogenation Other ... – PowerPoint PPT presentation

Number of Views:96
Avg rating:3.0/5.0
Slides: 74
Provided by: SteveH121
Category:

less

Transcript and Presenter's Notes

Title: Martyn Poliakoff


1
Catalyddion Aml-Ochrog mewn Hylyfoedd Uwchradd
  • Martyn Poliakoff
  • martyn.poliakoff_at_nottingham.ac.uk

2
Supercritical 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)

3
Critical Points
Pc
4
Supercritical Catalysis
  • Catalysis in scCO2- Hydrogenation,
    Hydroformylation
  • Supercritical Water
  • Biocatalysis

5
Miscibility 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.
6
Continuous Supercritical Hydrogenation
7
Other Hydrogenations successfullycarried out in
scCO2 and scPropane
8
scCO2 Chemical Plant opened July,2002
  • continuous
  • multipurpose
  • 1000 ton p.a.

Thomas Swan Co
9
Hydrogenation of Isophorone
The product by-products have similar boiling
points Conventional process requires an
expensive downstream separation
scCO2 - quantitative, no by-products
10
(No Transcript)
11
(No Transcript)
12
scCO2 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
13
Bi-phasic Catalysis Cole-Hamilton
P. B. Webb, M. F. Sellin, et al. J. Am. Chem.
Soc.,2003, 125, 15577
14
Green 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
15
Gas-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
17
Gas-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.

18
Hydrogenation of Isophorone
Reaction has a high space-time yield How is this
influenced by the phase behaviour of the system?
19
Isophorone /CO2/H2 phase boundaries
M. Sokolova Ke Jie
20
CO2- 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

21
Hydrogenation of sertraline imine in CO2expanded
THF
22
Commercial Route to Zoloft
23
Continuous hydrogenation of rac-sertraline in
scCO2/THF
  • Investigate both chemoselectivity
    diastereoselectivity
  • Aims (1) lt 1.5 dechlorination
  • (2) gt 928 de

P. Clark
24
Hydrogenation 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)
25
Summary
  • 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

26
Supercritical Catalysis
  • Catalysis in scCO2
  • Supercritical Water- Selective
    Oxidation, Formation of Caprolactam
  • Biocatalysis

27
Total 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

28
Johnson Matthey ChematurAquaCatProcess for
Catalyst Recoveryopened Oct 10th 2003
29
Heterogeneous Catalyst Recovery
Before
After
30
Partial 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)
31
Oxidation of p-Xylene
  • 0.7 Mton p.a. per plant
  • TA insoluble in CH3COOH
  • 18 of world production of CH3COOH lost in the
    process

32
(No Transcript)
33
TA
34
Oxidation of p-Xylene / scH2O
PA Hamley, et al. Green Chem. (2002) 4, 235
(2005) 7, 294
35
Oxidation of p-Xylene in scH2O
36
Selective 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

37
EXAFS Molecular Dynamics Results with 0.4 m
MnBr2
W. Partenheimer, Y. Chen, J. L. Fulton J. Am.
Chem. Soc. 127, 14086, (2005)
38
IR 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)
39
FTIR 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
40
High T P IR Cell Yu. E. Gorbaty
41
Hydrolysis of MeCN
42
(No Transcript)
43
Raman Spectroscopy
Eleni Venardou Appl. Spectrosc., (2003) 57
44
Raman Spectra of CH3CN in ncH2O
no added acid 300 C, 300 bar
45
Raman Spectra of CH3CN in ncH2O
46
Hydrolysis of MeCN Effect of Concentration
47
Caprolactam
  • Industrial synthetic route
  • Problem
  • 5 kg (NH4)2SO4 are made per kg CPL

48
Alternative Synthesis
  • Cheaper feedstock,
  • No cyclohexane oxidation
  • No ammonium sulphate

Yan Chong
49
(No Transcript)
50
Strategy
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

51
Caprolactam 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
52
Supercritical Catalysis
  • Catalysis in scCO2
  • Supercritical Water
  • Multiphasic Biocatalysis
  • Helen Hobbs, Neil Thomas

53
Enzymes in Fluorous Biphase
PFMC Perfluoro- Methyl Cyclohexane
54
How can one dissolve an enzyme in a fluorous
solvent (or even scCO2)?
55
Hydrophobic Ion Pairing
56
Fluorinated Anionic Surfactant
Krytox NH4 n 14/2500 KDP NH4 n 7/1400
Soluble in Fluorous phase and scCO2
57
Cytochrome c inaqueous buffer
58
Fluorous Phase added
Fluorous Krytox
59
HIP extraction into theFluorous Phase
Butis the enzyme really dissolved?
60
Dynamic Light Scattering Candida rugosa lipase
Expected Diameter 6.8 nm
61
KDP surfactant mw1400 Expected length 1.4 nm
62
Expected diameter 9.6 nm (CRL-KDP)
63
(No Transcript)
64
Biocatalysis in Fluorous Biphase
65
CMT-KDP Recycling (FBS)
66
Dissolving Biomolecules
  • Precipitation from aqueous buffer

Dissolve in scCO2
67
Biological Molecules in scCO2
Cytochrome C
68
Supercritical Catalysis
  • Continuous Reactions
  • Key aspect of supercritical fluids
  • New Developments Green technologies are not in
    competition
  • Partnership between Chemists Chemical Engineers

69
DICE 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

70
P 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
72
GSC-33rd International Conference on Green
Sustainable Chemistry
1-5 July 2007, Delft, The Netherlands
73
GSC-33rd International Conference on Green
Sustainable Chemistry
Professor Graham Hutchings RSC Green Chemistry
Lecturer
1-5 July 2007, Delft, The Netherlands
Write a Comment
User Comments (0)
About PowerShow.com