Heterogeneous Catalysis for Green Chemistry Dr. M. Sankar Cardiff Catalysis Institute School of Chemistry Cardiff University Cardiff, UK. 02/01/2010 Cardiff Catalysis Institute
Overview of this Presentation Organic Carbonates using CO 2 Synthesis of Cyclic Carbonates Synthesis of Dimethyl Carbonates Selective oxidation using Gold nanocrystals based Catalysts Oxidation of Benzyl Alcohol using Au-Pd Supported on TiO 2 Oxidation of Glycerol using supported monometallic Catalysts.
Mt. Kilimanjaro (Africa ). Ice cap is shrinking Columbia glacier Alaska Glacier National Park Global Warming – Visible Effects
CO 2 Emission & Possible Solution Sequestration Utilization M. A. Scibioh, B. Viswanathan Proc.Indn.Natl.Acad.Sci., 70A (3), 2004.
Various Chemical Transformations using CO 2 Monomers Aprotic Organic Solvents Fine Chemical Intermediates Cyclic Carbonate Methylating Agent Carbonylating Agent Oxygenated fuel additive Substitute for MTBE Dimethyl Carbonate
Specific Reactions of Interest Cyclic Carbonate Dimethyl Carbonate
Synthesis of Cyclic Carbonates
+ Catalytic System-I Na 12 [WZn 3 (H 2 O) 2 (ZnW 9 O 34 ) 2 ]46H 2 O (Zn-W-Sandwich Polyoxometalate) Dimethylaminopyridine
Experimental conditions: 0.4 MPa CO 2, 10 ml CH 2 Cl 2, mmol of Zn-POM, DMAP = 3 mole equivalent Zn POM Typical Reaction Data Substrate Product Temp (deg C) Time (Hrs) Conv (%) Selectivity (%)
Experimental conditions: 0.4 MPa CO 2, mmol of Zn-POM, DMAP = 3 mole equivalent Zn POM Data Continued……. SubstrateTemp (deg C) Time (Hrs) Conv (%) Selectivity(%) (without solvent) (Recovered POM)
Experimental conditions: 0.4 MPa CO 2, 10 ml CH 2 Cl 2, mmol of Zn-POM, DMAP = 3 mole equivalent Zn POM Data Continued….. SubstrateSub: Cat ratio Temp (deg C) Time (Hrs) Conv (%) Selectivity (%) 10, , ,
Structural Integrity of Zinc - Polyoxometalate
Proposed mechanism
Very high Substrate Vs Catalyst Ratio Reaction without organic solvent – atom economy Applicable to a range of epoxides Polyoxometalate part is Recoverable and reusable First ever Polyoxometalate based catalyst system for this particular reaction Highlights M. Sankar, N. Tarte, P. Manikandan, Appl. Catal. A. 276 (2004) p.217. US Patent - 6,924,379 Indian Patent - Granted
Catalytic System-II Si Si-O Si-O Si-O N N Si Si-OH Si-O Si-O N N OH I II and/or Si EtO EtO EtO NH N Si-OH Si-OH Si-OH + Silica Cl + Chloropropyl triethoxy silane Imidazole L. T. Aany Sofia, Asha Krishnan, M. Sankar, N. K. Kala Raj, P. Manikandan, P. R. Rajamohanan, and T. G. Ajithkumar* J. Phys. Chem. C 113 (2009),
Si-NMR of Fumed SilicaSi-NMR of Functionalised Silica Solid State NMR Characterization
13 C NMR of Functionalised Silica
Reaction Data Temperature EffectRecycle Studies
Catalyst Epoxide Temp/TimeEpox ConvCC Selec Si-ImidECH120 °C/4 h98 No CatalystECH120 °C/4 h<50 Si-ImidPO130 °C/10 h99 Si-ImidBO130 °C/10 h9994 Si-ImidSO130 °C/10 h7997 ECHPO BO SO Catalyst Activity
Structural Stability – MAS-NMR 13 C 29 Si Fresh Recovered Fresh Recovered
Proposed - Mechanism M.Sankar et.al., (Manuscript under preparation)
Highlights Single Site – Heterogeneous Catalyst Recoverable and Reusable Easy to synthesize Relatively mild reaction condition
CO 2 : 6-10 bar, Temp: ºC, Time: 4-10 h Yield : > 96 %, Solvent:No Recoverable & Reusable: Yes R = H, Cl, CH 3 Cyclic Carbonate Summary
Synthesis of Dimethyl carbonate
Exp. Cond. EC/PC : 50mmol, Methanol : 500mmol Catalyst: 1gm p-Xylene : 1gm Time: 5hrs Sl. No. Subs Catalyst Temp o C DMC Yield(%) 1ECNa 2 WO 4.2H 2 O2579 2ECNa 2 WO 4.2H 2 O (I-Recov) PCNa 2 WO 4.2H 2 O2523 4ECCaWO ECLi 2 WO ECK 2 WO ECNa 2 VO Catalytic System-I
Catalysis Data Effect of TemperatureHeterogeneous Catalyst
Powder XRD IR Structural Integrity of Sodium Tungstate
Adsorbed CH 3 O - CH 3 OH Adsorbed CH 3 O - Active Intermediate: IR and Raman Studies
Proposed Mechanism DMC formation M. Sankar, N. Madhavan Nair, K.V.G.K. Murty, P. Manikandan, Appl. Catal. A. 312 (2006) p.108. US Patent – Applied Indian Patent - Applied
Highlights Active at room temperature No CO 2 pressure – pot reaction Recoverable & Reusable No complicated synthesis
Selective Oxidation using “Green” Oxidants Introduction: Au and Au-Pd nanoparticles based catalysts have been reported to be very effective for : Epoxidation of Alkenes: Hutchings et.al., Nature (2005). Direct synthesis of Hydrogen Peroxide: Hutchings et.al., Science (2009). Oxidation of Primary Alcohols: Hutchings et.al., Science (2006), In this Presentation: Oxidation of Benzyl Alcohol : Mechanistic Investigation Oxidation of Bio-renewable Feedstocks : Glycerol Oxidation
Benzyl alcohol conversion and selectivity in benzaldehyde with the reaction time at 100 o C, 0.2 MPa O 2 pressure: () Au/TiO 2, ( )Pd/TiO 2, ( ) Au-Pd/TiO 2 ; solid symbols – conversion, open symbols – selectivity Science 2006 AuPd nanoparticles prepared by impregnation 1-50 nm Au-rich core, Pd-rich surface Oxidation of Benzyl Alcohol using Au-Pd supported on TiO 2 Aim is to understand the origin of Toluene in the “Solventless” oxidation of Benzyl alcohol and thereby “switching off” the toluene production
Experimental 50 ml Glass Reactor Stirred at 1000 rpm – No mass transport limitations Analysed by GC using mesitylene as external standard Rates of the reaction were calculated for the first 10% conversion level Catalyst Synthesis: (Au-Pd)/TiO 2, Au/TiO 2, Pd/TiO 2 by Sol-immobilization technique 1 Catalytic Reaction (3 phase system: solid/liquid/gas) 1 J.A. Lopez-Sanchez, N. Dimitratos, P. Miedziak, E. Ntainjua, J.K. Edwards, D. Morgan, A.F. Carley, R. Tiruvalam, C.J. Kiely and G.J. Hutchings, Phys.Chem. Chem. Phys, 2008, 10, 1921.
Initial rates of reaction under oxygen at 80 o C CatalystBenzyl AlcoholBenzaldehydeToluene d[BzOH]/dt ( mol s -1 ) R2R2 d[Ald]/dt ( mol s -1 ) R2R2 d[Tol]/dt ( mol s -1 ) R2R2 1%(Au-Pd)/TiO ± ± ± %Au/TiO ± ± ± %Pd/TiO ± ± ± Catalyst: 0.02g Benzyl Alcohol: 1g O 2 : 1 bar Stirring: 1000rpm Initial rates of reaction under He at 80 o C CatalystBenzyl AlcoholBenzaldehydeToluene d[BzOH]/dt ( mol s -1 ) R2R2 d[Ald]/dt ( mol s -1 ) R2R2 d[Tol]/dt ( mol s -1 ) R2R2 1%(Au-Pd)/TiO ± ± ± %Au/TiO ± ± ± %Pd/TiO ± ± ± Catalyst: 0.02g Benzyl Alcohol: 1g He: 1 bar Stirring: 1000rpm Monometallic versus Bimetallic Catalysts No reaction in the absence of catalyst
Reaction of PhCH 2 OH versus PhCD 2 OH Rate of disappearance of benzyl alcohol ▲(Proton) ● (Deuterated) under 1 bar He Under Oxygen (1 bar) SubstrateBenzyl AlcoholBenzaldehydeToluene d[BzOH]/dt ( mol s -1 ) R2R2 d[Ald]/dt ( mol s -1 ) R2R2 d[Tol]/dt ( mol s -1 ) R2R2 PhCH 2 OH-5.42 ± ± ± PhCD 2 OH-2.05 ± ± ± KIE Substrate: 1g Catalyst: 0.02g O 2 : 1bar Stirring: 1000 rpm Temp: 80 o C
Deuterium NMR (coupled) of the reaction mixture (inset toluene peak magnified)
GC- Mass analysis of the reaction mixture – Comparison of protonated toluene and deuterated toluene part alone shown for clarity.
Effect of atmosphere on the initial rate of reaction Gas/PressBenzyl AlcoholBenzaldehydeToluene d[BzOH]/dt ( mol s -1 ) R2R2 d[Ald]/dt ( mol s -1 ) R2R2 d[Tol]/dt ( mol s -1 ) R2R2 He ± ± ± Air ± ± ± O 2 / 1 bar ± ± ± O 2 / 2 bar ± ± ± O 2 / 3 bar ± ± ± Benzyl Alcohol : 1g Catalyst: 0.02g Temp: 80 o C Stirring: 1000 rpm Pressure: 1bar
Effect of dilution with o-xylene Lineweaver-Burk plot of initial rates versus formal concentration of benzyl alcohol Derive v max & K d K d ald << K d tol Active site for the two products Appears to be different
PhCH 2 H C HOPh H C PhHO O O. H CO O. PhH H HO H H PHePO1 PO2 Speculation on mechanism & structure of precursor states PhCH 2 OH PhCH 2 OH CAT PHe PhCHO PhCH 3 PhCH 2 OH/O 2 CAT PO1 PO2 PhCHO PhCH 3 O 2 He M. Sankar et.al., Faraday Discussions, 2009 (In Press)
Glycerol Oxidation – Possible Products
Oxidation of Glycerol in an autoclave reactor using O 2 or aq. H 2 O 2 M.Sankar, N. Dimitratos,D. W. Knight, A. F. Carley,R. Tiruvalam,C. J. Kiely, D.Thomas,and G. J. Hutchings*, ChemSusChem, 2010 (In press)
Acknowledgements Dr. P. Manikandan, NCL Pune Prof. Graham J Hutchings, Cardiff University Prof. David W Knight, Cardiff University Prof. Donald Bethell, Liverpool University Dr. S. Sivasanker, NCCR, Chennai Prof. B. Viswanathan, NCCR, Chennai EPSRC & CSIR