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Enter title of presentation here Enter author’s names here   If University Logo is required, please  adjust size to fit below the line, e.g. Hydrogen Spillover Effect  in the Fischer-Tropsch  Synthesis The role of platinum as a promoter on  cobalt-based catalysts Doreen Nabaho , Eric van Steen, Michael Claeys Centre for Catalysis Research, Department of Chemical Engineering University of Cape Town, Private Bag X3, Rondebosch, 7701, RSA E-mail :  [email_address]
Dry M.E. Hydrocarbon Processing 61 (1982) 121 - 124.  ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Low Temperature Fischer-Tropsch: Cobalt-based catalyst   Goal:  to elucidate the behaviour of the cobalt-based Fischer-Tropsch catalyst
Composition of patented cobalt-based catalysts ,[object Object],[object Object],[object Object],[object Object],[object Object],Oxide  Promoter 1-10wt% Noble metal  promoter <0.1wt% Cobalt  15-30wt% Catalyst support Oukaci R., A.H. Singleton and J.G. Goodwin jr. Applied Catalysis A: General 186 (1999) 129-144
[object Object],[object Object],[object Object],Cobalt oxide (Co 3 O 4 ) crystallites 10-20nm Al 2 O 3  support  particle ~150 μ m  Cobalt-based Fischer-Tropsch catalyst   ,[object Object],[object Object],[object Object],[object Object],[object Object],1 Morales, F., and B.M. Weckhuysen: Catalysis, Vol. 19. Royal Society of Chemistry, Cambridge.  Metallic cobalt crystallites(Co 0 ) Reduction before Fischer-Tropsch synthesis  (H 2  )
Alumina How does platinum increase Fischer-Tropsch rate? ,[object Object],[object Object],[object Object],[object Object],[object Object],? 1 Morales, F., and B.M. Weckhuysen: Catalysis, Vol. 19. Royal Society of Chemistry, Cambridge.  Effects of Promoters 1 Co Pt ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],↑  number of ‘ active sites’ ↑  activity of each  ‘ active site’  Platinum increases Co 0  after reduction of Co 3 O 4  -> more active sites
Co 3 O 4  + 4H 2  -> 3Co + 4H 2 O Cobalt oxide (Co 3 O 4 ) Alumina support  higher rate increases vs. unpromoted catalyst due to increase in Co 0  Limited proof of hydrogen spillover on platinum promoted cobalt-based catalysts available in reviewed literature Q: BUT how exactly does platinum increase metallic cobalt?  A: Often postulated to be due to a  HYDROGEN SPILLOVER MECHANISM  Mechanism of structural promotion with platinum  ,[object Object],[object Object],[object Object],[object Object],[object Object],Metallic cobalt crystallites (Co 0 )  Reduction in H 2  at 300-450 o C Platinum
Promotion with platinum:   Hydrogen spillover mechanism ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Definition: The dissociative chemisorption of hydrogen molecules on metal surfaces to form adsorbed hydrogen species (H*) followed by their migration to another surface. 1 1 Roland U., Braunschweig T. and Roessner F.  Journal of Molecular Catalysis A: Chemical 127 (1997), 61-84
1 Claeys M. and van Steen E.: “Basic studies in Fischer-Tropsch Technology” (A.P. Steynberg, M.E. Dry, Eds.),  Studies in Surface Science and Catalysis 152 (2004), 601-680.  ,[object Object],[object Object],Alumina metallic  cobalt gaseous  H 2   molecules ,[object Object],[object Object],[object Object],The Fischer-Tropsch Synthesis:  Hydrogen spillover ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Pt Could  dissociated hydrogen  FROM PLATINUM  spillover  TO COBALT  during the Fischer-Tropsch Synthesis? Cobalt oxide ,[object Object],[object Object],[object Object]
[object Object],cobalt oxide (Co 3 O 4 ) alumina support  platinum promoted cobalt  catalyst platinum catalyst cobalt catalyst platinum promoter Experimental methodology:  Hybrid catalysts  ,[object Object],[object Object],[object Object],[object Object],[object Object]
Experimental Methodology:  Catalysts ,[object Object],[object Object],[object Object],[object Object],[object Object],‘ Hybrid’ Pt-Co  Co/ γ- Al 2 O 3 Pt/ γ- Al 2 O 3 Prepared by slurry impregnation Precursors:  Co(NO 3 ) 2   Pt[(NH 3 ) 4 ]Cl 2   Pt:Co  mass ratio =  1:40 ‘ co-impregnated’ Pt-Co/ γ- Al 2 O 3
Catalyst characterisation ,[object Object],[object Object],[object Object],[object Object],[object Object],Co 3 O 4  clusters d cluster  = 150-200 nm d crystallite ,TEM = 7-9 nm d crystallite ,XRD = 9.3 nm (Co/Al 2 O 3 ) & 9.6nm (Pt-Co/Al 2 O 3 ) Pt/Al 2 O 3 50nm 100nm Pt-Co/Al 2 O 3 200nm Co/Al 2 O 3  Pt crystallites d crystallite,TEM  = 1-2 nm d crystallite,COchem   = 1.9 nm Prepared loading (wt%) Co/Al 2 O 3   Pt-Co/Al 2 O 3   Cobalt 19.4 19.4 Platinum - 0.5 Pt/Al 2 O 3   - 0.5
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Experimental Methodology: Summary of experiments ,[object Object],[object Object],[object Object],[object Object],[object Object],Investigating H 2  Spillover in the Fischer-Tropsch Synthesis  During Co 3 O 4  reduction During Fischer-Tropsch synthesis
H 2  Spillover during reduction:   Temperature Programmed Reduction (TPR)  ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Co 3 O 4  + 4H 2  -> 3Co + 4H 2 O MILL
Catalyst Characterisation:  XRD ,[object Object],[object Object],[object Object],[object Object],[object Object],Co/Al 2 O 3 (milled) Radiation source: Co K- α Hybrid Pt-Co (milled) Pt-Co/Al 2 O 3
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],H 2  Spillover during reduction:   Temperature Programmed Reduction (TPR)  Hydrogen consumption Co/Al 2 O 3  milled Hybrid Pt-Co milled Pt-Co/Al 2 O 3 Degree of Reduction (%Co 0 ) Co/Al 2 O 3 22.2 Pt-Co hybrid 87.9 Pt-Co/Al 2 O 3 97.8 Increasingly easier to reduce with Pt closer to Co Increasing trend in agreement with hydrogen spillover theory
Hydrogen Spillover during FT: Turn over numbers & product analysis ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Platinum is hardly active under these Fischer Tropsch conditions! Could surface be covered with carbon monoxide and thus hydrogen adsorption inhibited? 1 FID Chromatogram of Pt/Al 2 O 3 1 McKee D.W.  Journal of Catalysis  8 (1967), 240-249  Illustration Turn Over Number @80 h  (mmol CO /g Co . s) Co/Al 2 O 3 3.35 X 10 -2 Pt/Al 2 O 3 n/a Hybrid Pt-Co  (Pt/Al 2 O 3  + Co/Al 2 O 3 ) 3.53 X 10 -2 Pt-Co/Al 2 O 3   3.15 x 10 -2 C 1 +C 2 Reference gas: cyclohexane
Hydrogen Spillover during FT:   Olefin content in product ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Co/Al 2 O 3 Pt-Co hybrid Pt-Co/Al 2 O 3 olefin content in linear hydrocarbons and 1-olefin content in linear olefins (@ X CO =20%) similar and thus unaffected by platinum
[object Object],[object Object],[object Object],[object Object],[object Object],  Hydrogen Spillover during FT:  Anderson-Schulz-Flory distribution Determined  from C 4 -C 10
Hydrogen Spillover in the Fischer-Tropsch Synthesis: A summary ,[object Object],[object Object],[object Object],[object Object],[object Object],Fischer-Tropsch so far: Platinum is hardly active under these Fischer-Tropsch conditions & also doesn’t affect product selectivity in promoted or unpromoted catalysts Platinum inactivity likely due to strong carbon monoxide adsorption ->platinum surface not accessible to hydrogen making spillover unlikely Further work: in-situ XRD to obtain better Co 0  estimates for Turn Over Number, cobalt oxide reduction peak identification, characterisation of spent catalysts.  Contribution to Catalysis Research: - understanding spillover effects during  catalyst reduction and Fischer-Tropsch synthesis - Add to limited understanding of promoters in Cobalt-based catalysts to enable better catalyst design  Platinum increases  the Fischer-Tropsch rate by increasing degree of reduction of cobalt catalysts. Mechanism suspected to be via hydrogen spillover and TPR results obtained so far point to this
ACKNOWLEDGEMENTS Insert University Collaboration Logo’s Here, e.g. Questions &  Comments? Department of Science and Technology
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Gold Promoters for Cobalt-based Catalysts  ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],? H 2   probably in RDS

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Doreen Nabaho Cchange&amp;Catsa9 Nov

  • 1. Enter title of presentation here Enter author’s names here If University Logo is required, please adjust size to fit below the line, e.g. Hydrogen Spillover Effect in the Fischer-Tropsch Synthesis The role of platinum as a promoter on cobalt-based catalysts Doreen Nabaho , Eric van Steen, Michael Claeys Centre for Catalysis Research, Department of Chemical Engineering University of Cape Town, Private Bag X3, Rondebosch, 7701, RSA E-mail : [email_address]
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  • 20. ACKNOWLEDGEMENTS Insert University Collaboration Logo’s Here, e.g. Questions & Comments? Department of Science and Technology
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Editor's Notes

  1. Carbon efficiency of GTL Plant = 57-70% Vs 90% in refineries : http://www.fosterwheeler.com/publications/tech_papers/files/IChemE%20WCCE%2005%20LNG%20versus%20GTL.pdf http://findarticles.com/p/articles/mi_m0CYH/is_20_4/ai_67316759/ GTL Fuels burn more cleanly: http://www.ifandp.com/article/00210.html Fluctuating costs: Most of the plants that were proposed in Qatar have been cancelled (ConocoPhillips and Marathon in Qatar, and all other Nigerian plants) or converted to LNG projects (ExxonMobil’s plant in Qatar). Energy intensive so that the plant is using 40% of the gas Advances in cat tech have helped inspite of this process being expensive + energy intensive
  2. Oukaci et al. (1999) carried out an overview of the current generation of patented cobalt-based Fischer-Tropsch catalysts. A summary of the general chemical characteristics of the catalysts that were reviewed is shown in Table 1. give e.g of oxide, support,noble metal
  3. Vannice, 1975; van Santen et al. -in press) (Weng et al., 1992; Delmon et al., 1994; Baeza et al., 2006)
  4. with Pt, Co 3 O 4 reduce at lower T &amp; so a larger fraction form Co 0 at reduction conditions higher degree of reduction results in a higher dispersion and thus higher activity
  5. Surface mobility of reacting species and intermediates is a well known phenomenon and has been observed for other compounds such as oxygen, carbon monoxide, nitrogen and even organic species over distances of up to several millimeters (Weng et al., 1992; Delmon et al., 1994; Baeza et al., 2006).
  6. Based on the properties of spillover hydrogen, it was expected that during reduction, hydrogen would initially dissociate on the platinum surface to alumina from where secondary spillover would occur to the cobalt surface and induce reduction.
  7. Mentioned that catalysts are unreduced here.
  8. Say: for the sake of today’s study, I’d like to present the results this way…
  9. Briefly talk about peak identification
  10. NB: Prior to Fischer-Tropsch: Non-hybrid catalyst samples (Co/Al 2 O 3 , Pt/Al 2 O 3 ) also crushed in micronising mill for consistency in comparison with Pt-Co hybrid Degree of Reduction calculated based on milled catalysts
  11. DOR needed for TON When I refer to hybrid I mean milled
  12. TON calculated based on loaded amount of cobalt
  13. Further indication of possible saturation of platinum surface by carbon monoxide
  14. Points to CO hydrogenation
  15. Due to exp relationship Precovered by other intermediates It is therefore likely that hydrogen is involved in the rate determining step of the Fischer-Tropsch synthesis; meaning that one could effectively increase the reaction rate by delivering more hydrogen to the active surface during Fischer-Tropsch by hydrogen spillover. A point to note is that when delivering more hydrogen to the active surface, there is a trade-off between increasing the olefin readsorption and thus chain growth (an advantage) versus primary hydrogenation which would have the unwanted effect of decreasing the C 5+ selectivity.