Cr/SiO2 catalysts (Cr loading in the 0.25-2.0 wt% range) have been prepared by direct hydrothermal synthesis in the presence of templating agents, in order to attain porous systems with high specific surface area (in the 600-1000 m(2) g(-1) range), and then characterized and tested in the oxidative dehydrogenation of propane in the presence of CO2 or CO2 + O-2 as an oxidant. The extent and regularity of mesopores decreased significantly by increasing the Cr content (X-ray diffraction, N-2 adsorption, transmission electron microscopy), but this did not limit the catalytic performances of the catalysts with higher Cr loadings. In all cases, the only chromium species found were surface chromates (diffuse reflectance electronic spectroscopy and X-ray absorption near edge spectroscopy), accompanied by Bronsted acid centres (infrared spectra of adsorbed NH3). All catalysts appeared stable towards irreversible deactivation, even after ca. 900 min of testing, and propene yields as high as 40% were attained. The combination of spectroscopic and catalytic results allowed us to rationalize, at least in part, the role of different oxidants in defining the chromium oxidation state, and a tentative correlation of the oxidation state of Cr species during the reaction (Cr2+/Cr3+) with selectivity to propene is suggested.

Towards efficient catalysts for the oxidative dehydrogenation of propane in the presence of CO2: Cr/SiO2systems prepared by direct hydrothermal synthesis

BOTAVINA, Maria;GROPPO, Elena Clara;MARTRA, Gianmario
2016-01-01

Abstract

Cr/SiO2 catalysts (Cr loading in the 0.25-2.0 wt% range) have been prepared by direct hydrothermal synthesis in the presence of templating agents, in order to attain porous systems with high specific surface area (in the 600-1000 m(2) g(-1) range), and then characterized and tested in the oxidative dehydrogenation of propane in the presence of CO2 or CO2 + O-2 as an oxidant. The extent and regularity of mesopores decreased significantly by increasing the Cr content (X-ray diffraction, N-2 adsorption, transmission electron microscopy), but this did not limit the catalytic performances of the catalysts with higher Cr loadings. In all cases, the only chromium species found were surface chromates (diffuse reflectance electronic spectroscopy and X-ray absorption near edge spectroscopy), accompanied by Bronsted acid centres (infrared spectra of adsorbed NH3). All catalysts appeared stable towards irreversible deactivation, even after ca. 900 min of testing, and propene yields as high as 40% were attained. The combination of spectroscopic and catalytic results allowed us to rationalize, at least in part, the role of different oxidants in defining the chromium oxidation state, and a tentative correlation of the oxidation state of Cr species during the reaction (Cr2+/Cr3+) with selectivity to propene is suggested.
2016
6
3
840
850
CHROMIUM-OXIDE CATALYSTS; DIFFUSE-REFLECTANCE SPECTROSCOPY; CARBON-DIOXIDE; LIGHT ALKANES; SUPPORTED CATALYSTS; IN-SITU; ETHYLENE POLYMERIZATION; VANADIUM-OXIDE; ACTIVE-SITES; CR-MCM-41
Botavina, M. A.; Agafonov, Yu. A.; Gaidai, N. A.; Groppo, E.; Cortés Corberán, V.; Lapidus, A. L.; Martra, G.
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/2318/1570273
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