TY - JOUR
T1 - Time-resolved operando X-ray absorption study of CuO-CeO2/Al2O3 catalyst during total oxidation of propane
AU - Alexopoulos, Konstantinos
AU - Anilkumar, Mettu
AU - Reyniers, Marie Françoise
AU - Poelman, Hilde
AU - Cristol, Sylvain
AU - Balcaen, Veerle
AU - Heynderickx, Philippe M.
AU - Poelman, Dirk
AU - Marin, Guy B.
PY - 2010/6/18
Y1 - 2010/6/18
N2 - The local structure of the copper phase of a CuO-CeO2/Al2O3 catalyst and its activity for the total oxidation of propane have been studied under working conditions, using time-resolved X-ray absorption spectroscopy (XAS) in transmission mode at the Cu K edge coupled with on-line mass spectrometry (MS). In the temperature range of 573-723 K, the copper phase of the catalyst remains oxidized (i.e. Cu2+) during total oxidation reaction conditions (1%C3H8-5%O2/He), while three species are present (i.e. Cu2+, Cu1+ and Cu0) during reduction (2%C3H8/He) and re-oxidation (10%O2/He) treatments where a two-step mechanism is found. Catalyst reduction is fully reversible, as the Cu2+ nature of the catalyst is recovered after a reduction-oxidation cycle. Re-oxidation of the catalyst is two orders of magnitude faster than its reduction and has an apparent activation energy of 24 kJ/mol. On the other hand, catalyst reduction requires an apparent activation energy of 70 kJ/mol, which is equal to the apparent activation energy determined under total oxidation reaction conditions. These results give support to a Mars-van-Krevelen reaction scheme with the copper phase of the catalyst being close to a fully oxidized state.
AB - The local structure of the copper phase of a CuO-CeO2/Al2O3 catalyst and its activity for the total oxidation of propane have been studied under working conditions, using time-resolved X-ray absorption spectroscopy (XAS) in transmission mode at the Cu K edge coupled with on-line mass spectrometry (MS). In the temperature range of 573-723 K, the copper phase of the catalyst remains oxidized (i.e. Cu2+) during total oxidation reaction conditions (1%C3H8-5%O2/He), while three species are present (i.e. Cu2+, Cu1+ and Cu0) during reduction (2%C3H8/He) and re-oxidation (10%O2/He) treatments where a two-step mechanism is found. Catalyst reduction is fully reversible, as the Cu2+ nature of the catalyst is recovered after a reduction-oxidation cycle. Re-oxidation of the catalyst is two orders of magnitude faster than its reduction and has an apparent activation energy of 24 kJ/mol. On the other hand, catalyst reduction requires an apparent activation energy of 70 kJ/mol, which is equal to the apparent activation energy determined under total oxidation reaction conditions. These results give support to a Mars-van-Krevelen reaction scheme with the copper phase of the catalyst being close to a fully oxidized state.
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U2 - 10.1016/j.apcatb.2010.04.022
DO - 10.1016/j.apcatb.2010.04.022
M3 - Article
AN - SCOPUS:77953126762
SN - 0926-3373
VL - 97
SP - 381
EP - 388
JO - Applied Catalysis B: Environmental
JF - Applied Catalysis B: Environmental
IS - 3-4
ER -