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Silica and zirconia supported catalysts for the low-temperature ethanol steam reforming
被引:77
作者:
Rossetti, Ilenia
[1
,2
]
Lasso, Jose
[1
,2
]
Nichele, Valentina
[3
,4
]
Signoretto, Michela
[3
,4
]
Finocchio, Elisabetta
[5
,6
]
Ramis, Gianguido
[5
,6
]
Di Michele, Alessandro
[7
]
机构:
[1] Univ Milan, INSTM Unit, Dip Chim, I-20133 Milan, Italy
[2] CNR ISTM, I-20133 Milan, Italy
[3] Univ Ca Foscari Venezia, Dip Sci Mol & Nanosistemi, I-2137 Venice, Italy
[4] INSTM Unit Venezia, I-2137 Venice, Italy
[5] Univ Genoa, Dip Ingn Civile Chim & Ambientale, I-16129 Genoa, Italy
[6] INSTM Unit Genova, I-16129 Genoa, Italy
[7] Univ Perugia, Dip Fis, I-06123 Perugia, Italy
关键词:
Ethanol steam reforming;
H-2;
production;
Ni catalysts;
Silica;
Zirconia;
Catalyst deactivation;
Coking;
NI CRYSTAL SIZE;
NI/ZRO2;
CATALYSTS;
HYDROGEN-PRODUCTION;
PARTIAL-OXIDATION;
SBA-15;
CARBON;
SURFACE;
PERFORMANCES;
NANOTUBES;
ISSUES;
D O I:
10.1016/j.apcatb.2013.12.012
中图分类号:
O64 [物理化学(理论化学)、化学物理学];
学科分类号:
070304 ;
081704 ;
摘要:
Ethanol steam reforming has been investigated in the low temperature range, focusing not only on H-2 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 degrees 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. (C) 2013 Elsevier B.V. All rights reserved.
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页码:257 / 267
页数:11
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