330120 Catalytic Consequences of Reactive Intermediates During Partial Oxidation of Methanol On Pt Clusters
Catalytic Consequences of Reactive Intermediates during Partial Oxidation of Methanol on Pt Clusters
Weifeng Tu1,2 and Ya-Huei (Cathy) Chin1,*
1 Department of Chemical Engineering and Applied Chemistry, University of Toronto, Toronto, Canada
2 College of Power Engineering, Chongqing University, Chongqing, China
(*) corresponding author: cathy.chin@utoronto.ca
Keywords: methanol oxidation, Pt, partial oxidation, alcohol, formaldehyde, chemisorbed oxygen, oxygen binding strengths
Reactions of alkanol and oxygen over transition metal or metal-oxide catalysts lead to value added products of aldehydes and esters, syngas, or combustion products (CO2, H2O) at rates and selectivities that vary largely with the operating oxidant-to-alkanol ratios, because these ratios prescribe the chemical state of catalytic sites and the identity and coverages of reactive intermediates on Pt cluster surfaces during steady-state catalysis. The effects of surface coverages of the diverse intermediates and their relative abundances on supported Pt clusters are interpreted here in terms of oxygen and carbon virtual pressures, the rigorous surrogates of their respective chemical potentials, and connected to the rates and selectivities of methanol partial oxidation based on rate measurements at differential conditions and elimination of transport artifacts by extensive dilution within the intra-pellet and catalytic bed.
CH3OH-O2 catalytic turnovers (O2/CH3OH=0.1-40; 353-473 K) on Pt clusters (1.5-10 nm) form CH2O, CH3OCHO, CO2, and H2O. The catalytic reactions do not form CO and H2 at detectable limits under all conditions before the complete depletion of O2 because O2 reactions with CO and H2 are much faster than with CH3OH. The primary and secondary nature of the CH2O, CH3OCHO, and CO2 product and the relative rates of their reactions with oxygen relative to those of CH3OH were probed from CH3OH-O2, CH2O-O2, and CH3OCHO-O2 reactions at different oxidant-to-reductant ratios. The rates of CH3OCHO oxidation were unimportant relative to the CH3OH oxidation turnovers at Pt cluster surfaces occupied by chemisorbed oxygen (O*) and oxygenated intermediates (e.g. CH3O*) to varying extents. In contrast, CH2O oxidation rates became increasingly important relative to CH3OH oxidation rates as Pt cluster surfaces became populated with chemisorbed oxygen atoms. These results suggest that chemisorbed oxygen atoms are effective for oxidizing CH2O and CH3OH and become more reactive towards CH2O than CH3OH as they are more weakly bound at high surface coverages.
The individual rates of CH2O, CH3OCHO, and CO2 formation from CH3OH-O2 reaction acquire diverse kinetic dependencies with O2 and CH3OH pressures that can be categorized in three kinetic regimes according to the operating O2-to-CH3OH ratio, because this ratio influences the oxygen and carbon chemical potential at Pt cluster surfaces and thus, determines the relative abundances of the various reactive species of chemisorbed oxygen, unoccupied metal site, and methanol derived intermediates on Pt cluster surfaces. The identity and coverages of the reactive intermediates define the kinetically relevant steps during methanol partial oxidation and, in turn, lead to complex kinetic dependencies for the formation of CH2O, CH3OCHO, and CO2. At high O2/CH3OH ratios (> 7.5; 373 K), Pt cluster surfaces are saturated with reactive oxygen species; thus, CH2O, CH3OCHO, and CO2 formation rates do not vary with O2 pressure but increase with increasing CH3OH pressure. As the O2/CH3OH ratio decreases to intermediate values between 0.5 and 7.5 (373 K), kinetic dependencies for all products undergo a drastic transition: HCHO and CO2 formation rates are no longer proportional to CH3OH but instead acquire a linear dependence on O2 pressure and the CH3OCHO formation rates increase more than linearly with O2 pressure. Such kinetic transitions reflect a concomitant surface transition from O* saturation to uncovered of reactive intermediates, and from catalytic involvements of O* in CH3OH oxidation to * in O2 activation as the kinetically relevant step. As the O2/CH3OH ratio decreases further to below 0.5 (373 K), rates for CH2O and CO2 formation decrease with increasing CH3OH pressure but the rate for CH3OCHO is unaffected by CH3OH pressure. All of the species formation rates acquire a much larger dependence on O2 pressure with apparent reaction orders exceeding 1.5. These kinetic dependencies on CH3OH and O2 pressures are consistent with CH3OH activation at vacancies on Pt cluster surfaces that are saturated with CH3OH derived intermediates, prevalent only at the very low O2/CH3OH ratio.
The complex kinetic phenomena reported here are prescribed strictly by the operating O2-to-CH3OH ratio because the ratio determines the oxygen and carbon virtual pressures at the Pt cluster surfaces and in turn, the chemical states and identity and relative abundances of the surface intermediates during steady-state catalysis. Similar relations between the oxygen virtual pressure and the catalytic rate coefficients have been reported for alkane [1-2] and NO oxidation [3]. These relations appear to be ubiquitous for oxidation reaction on metal or metal-oxide clusters and govern the reaction path selectivities. <>Acknowledgements
We acknowledge China Scholarship Council for a Joint-Supervising Ph.D. program for Weifeng Tu and Natural Sciences Council of Canada (NSERC) and Canadian Foundation for Innovation (CFI) for their financial supports.
References
[1] Y-H. Chin, C. Buda, M. Neurock, and E. Iglesia, J. Am. Chem. Soc. 133 (2011) 15958.
[2] M. Garcia-Dieguez, Y-H. Chin, and E. Iglesia, J. Catal. 285 (2012) 260.
[3] B.M. Weiss and E. Iglesia, J. Phys. Chem. C 113 (2009) 13331.
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