MgO and Nb2O5 oxides used as supports for Ru-based catalysts for the methane steam reforming reaction

被引:16
作者
Amjad, Um-e-salma [1 ]
Lenzi, Giane Goncalves [2 ]
Camargo Fernandes-Machado, Nadia Regina [3 ]
Specchia, Stefania [1 ]
机构
[1] Dept Appl Sci & Technol, I-10129 Turin, Italy
[2] Univ Tecnol Fed Parana, Dept Chem Engn, BR-84016210 Ponta Grossa, PR, Brazil
[3] Univ Estadual Maringa, Dept Chem Engn, BR-98702090 Maringa, PR, Brazil
关键词
Magnesia; Niobic acid; Niobia; Ruthenium; Methane; Steam reforming; WATER-GAS SHIFT; HYDROGEN-PRODUCTION; PARTIAL OXIDATION; PREFERENTIAL OXIDATION; SURFACE-PROPERTIES; NIOBIC ACID; FUEL; XPS; ETHANOL; CO;
D O I
10.1016/j.cattod.2015.02.010
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A comparative analysis of Ru catalysts for low temperature (400-750 degrees C) methane steam reforming reaction has been performed on magnesia, niobic acid and niobia supports. Ru from chloride or nitrosyl nitrate precursors was deposited by incipient wetness impregnation method on supports calcined in different ways. All of the MgO-supported catalysts were calcined at 400 degrees C whilst the niobia-based catalysts underwent different calcinations regimes. The catalytic activity towards the methane steam reforming reaction was assessed in a fixed bed quartz reactor with an overall flow rate of 100 N cm(3) min(-1) (weight space velocity WSV of 33 N cm(3) min(-1) gc-al] and steam-to-carbon SIC ratio equal to 4). All of the catalysts showed comparable results, especially the magnesia- and the niobic acid-supported catalysts resulted in high activity at 700 degrees C, whereas a few of the niobia-supported catalysts achieved complete CH4 conversion. The best performing catalysts were characterized by BET, CO chemisorption, XRD, XPS and SEM analyses. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:122 / 130
页数:9
相关论文
共 65 条
[1]   Hydrogen from hydrocarbon fuels for fuel cells [J].
Ahmed, S ;
Krumpelt, M .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2001, 26 (04) :291-301
[2]  
Alonso CG, 2009, INT J CHEM REACT ENG, V7
[3]   Reactions over Cu/Nb2O5 catalysts promoted with Pd and Ru during hydrogen production from ethanol [J].
Alonso, Christian Goncalves ;
Furtado, Andreia Cristina ;
Cantao, Mauricio Pereira ;
Andreo dos Santos, Onelia Aparecida ;
Camargo Fernandes-Machado, Nadia Regina .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (08) :3333-3341
[4]   Comparative Study on Steam and Oxidative Steam Reforming of Methane with Noble Metal Catalysts [J].
Amjad, Um-E-Salma ;
Vita, Antonio ;
Galletti, Camilla ;
Pino, Lidia ;
Specchia, Stefania .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (44) :15428-15436
[5]   Characterization and dehydrogenation activity of Pt/Nb2O5 catalysts [J].
Aranda, DAG ;
Ramos, ALD ;
Passos, FB ;
Schmal, M .
CATALYSIS TODAY, 1996, 28 (1-2) :119-125
[6]   Magnesium salts and oxide: an XPS overview [J].
Ardizzone, S ;
Bianchi, CL ;
Fadoni, M ;
Vercelli, B .
APPLIED SURFACE SCIENCE, 1997, 119 (3-4) :253-259
[7]   Final step for CO syngas clean-up: Comparison between CO-PROX and CO-SMET processes [J].
Ashraf, Muhammad A. ;
Ercolino, Giuliana ;
Specchia, Stefania ;
Specchia, Vito .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2014, 39 (31) :18109-18119
[8]   Nb 3d and O 1s core levels and chemical bonding in niobates [J].
Atuchin, VV ;
Kalabin, IE ;
Kesler, VG ;
Pervukhina, NV .
JOURNAL OF ELECTRON SPECTROSCOPY AND RELATED PHENOMENA, 2005, 142 (02) :129-134
[9]   The relevance of Ru nanoparticles morphology and oxidation state to the partial oxidation of methane [J].
Balint, I ;
Miyazaki, A ;
Aika, K .
JOURNAL OF CATALYSIS, 2003, 220 (01) :74-83
[10]   Hydrogen production through sorption-enhanced steam methane reforming and membrane technology: A review [J].
Barelli, L. ;
Bidini, G. ;
Gallorini, F. ;
Servili, S. .
ENERGY, 2008, 33 (04) :554-570