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.
引用
收藏
页码:257 / 267
页数:11
相关论文
共 60 条
[1]  
[Anonymous], 1974, SELECTED POWDER DIFF, V1, P40
[2]   THE DETERMINATION OF PORE VOLUME AND AREA DISTRIBUTIONS IN POROUS SUBSTANCES .1. COMPUTATIONS FROM NITROGEN ISOTHERMS [J].
BARRETT, EP ;
JOYNER, LG ;
HALENDA, PP .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1951, 73 (01) :373-380
[3]   The role of surface reactions on the active and selective catalyst design for bioethanol steam reforming [J].
Benito, M. ;
Padilla, R. ;
Serrano-Lotina, A. ;
Rodriguez, L. ;
Brey, J. J. ;
Daza, L. .
JOURNAL OF POWER SOURCES, 2009, 192 (01) :158-164
[4]   COBALT-CATALYZED GROWTH OF CARBON NANOTUBES WITH SINGLE-ATOMIC-LAYERWALLS [J].
BETHUNE, DS ;
KIANG, CH ;
DEVRIES, MS ;
GORMAN, G ;
SAVOY, R ;
VAZQUEZ, J ;
BEYERS, R .
NATURE, 1993, 363 (6430) :605-607
[5]   CuiSiO2 and Cu/SiO2-TiO2 catalysts I.: TEM, DR UV-Vis-NIR, and FTIR characterisation [J].
Boccuzzi, F ;
Coluccia, S ;
Martra, G ;
Ravasio, N .
JOURNAL OF CATALYSIS, 1999, 184 (02) :316-326
[6]   Ex-nitrate Co/SBA-15 catalysts prepared with calibrated silica grains: Information given by TPR, TEM, SAXS and WAXS [J].
Boubekr, Fella ;
Davidson, Anne ;
Casale, Sandra ;
Massiani, Pascale .
MICROPOROUS AND MESOPOROUS MATERIALS, 2011, 141 (1-3) :157-166
[7]   Adsorption of gases in multimolecular layers [J].
Brunauer, S ;
Emmett, PH ;
Teller, E .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1938, 60 :309-319
[8]   FT-IR STUDY OF THE SURFACE OF COPPER-OXIDE [J].
BUSCA, G .
JOURNAL OF MOLECULAR CATALYSIS, 1987, 43 (02) :225-236
[9]   Opportunities and prospects in the chemical recycling of carbon dioxide to fuels [J].
Centi, Gabriele ;
Perathoner, Siglinda .
CATALYSIS TODAY, 2009, 148 (3-4) :191-205
[10]   Synthesis of carbon nanofibers:: effects of Ni crystal size during methane decomposition [J].
Chen, D ;
Christensen, KO ;
Ochoa-Fernández, E ;
Yu, ZX ;
Totdal, B ;
Latorre, N ;
Monzón, A ;
Holmen, A .
JOURNAL OF CATALYSIS, 2005, 229 (01) :82-96