Ethanol steam reforming has been investigated in the low temperature range, focusing not only on H2 productivity, but also on catalyst stability, very critical parameters under such conditions. Different supports (SiO2 and ZrO2), active phases (Ni, Co, Cu) and reaction temperature (300–500 °C) have been employed. Ni confirmed the best performing active phase to promote ethanol decomposition and reforming already at low reaction temperature. However, stability towards coking remains a key problem. The support plays a key role from this point of view. Indeed, the stabilization of the active phase in very dispersed form allowed to reach stable catalyst performance with time-on-stream. SiO2, thanks to no Lewis acidity and sufficiently strong metal–support interaction, demonstrated an interesting support for Ni under the selected operating conditions.

Silica and zirconia supported catalysts for the low-temperature ethanol steam reforming / I. Rossetti, J. Lasso, V. Nichele, M. Signoretto, E. Finocchio, G. Ramis, A. Di Michele. - In: APPLIED CATALYSIS. B, ENVIRONMENTAL. - ISSN 0926-3373. - 150(2014), pp. 257-267.

Silica and zirconia supported catalysts for the low-temperature ethanol steam reforming

I. Rossetti
;
J. Lasso
Secondo
;
2014

Abstract

Ethanol steam reforming has been investigated in the low temperature range, focusing not only on H2 productivity, but also on catalyst stability, very critical parameters under such conditions. Different supports (SiO2 and ZrO2), active phases (Ni, Co, Cu) and reaction temperature (300–500 °C) have been employed. Ni confirmed the best performing active phase to promote ethanol decomposition and reforming already at low reaction temperature. However, stability towards coking remains a key problem. The support plays a key role from this point of view. Indeed, the stabilization of the active phase in very dispersed form allowed to reach stable catalyst performance with time-on-stream. SiO2, thanks to no Lewis acidity and sufficiently strong metal–support interaction, demonstrated an interesting support for Ni under the selected operating conditions.
Catalyst deactivation; Coking; Ethanol steam reforming; H2 production; Ni catalysts; Silica; Zirconia
Settore CHIM/02 - Chimica Fisica
Settore CHIM/04 - Chimica Industriale
Settore ING-IND/25 - Impianti Chimici
2014
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/2434/235023
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