Preparation and characterization of Ru/MgO-Al2O3 catalysts for methane steam reforming

被引:62
作者
Carvalho, Luciene Santos [1 ,2 ]
Martins, Andre Rosa [1 ]
Reyes, Patricio [3 ]
Oportus, Marcelo [3 ]
Albonoz, Alberto [4 ]
Vicentini, Valeria [5 ]
Rangel, Maria do Carmo [1 ]
机构
[1] Univ Fed Bahia, Inst Quim, GECCAT, BR-40170290 Salvador, BA, Brazil
[2] UE Camacari, Ctr Fed Educ Tecnol Bahia, Dept Ensino, BR-42800000 Camacari, BA, Brazil
[3] Univ Concepcion, Fac Ciencias Quim, Concepcion, Chile
[4] Inst Venezolano Invest Cient, Ctr Quim, Caracas 21827, Venezuela
[5] Oxiteno SA Ind & Comercio, BR-09380440 Sao Paulo, Brazil
关键词
Steam reforming; Hydrogen production; Ruthenium catalyst; Mg-Al oxide; HYDROGEN-PRODUCTION; PARTIAL OXIDATION; MIXED OXIDES; GAS-PHASE; RU/AL2O3; ALUMINA; REDUCTION; SURFACE; AREA;
D O I
10.1016/j.cattod.2009.01.010
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The preparation and characterization of aluminum and magnesium oxides-supported ruthenium were described in this work, aiming to compare different supports to methane steam reforming catalysts for producing hydrogen. Gama-alumina-supported ruthenium and periclase-supported ruthenium were produced. The addition of small amounts of magnesium to alumina-supported ruthenium in the range of Mg/Al (molar)= 0.2-0.5 did not change the gama-alumina structure while high amounts (Mg/Al (molar) = 5) led to the production of periclase. Magnesium caused a decrease of specific surface area of alumina-supported ruthenium catalysts and this effect increased with the amount of the metal in solids. Magnesium also decreased the acidity of alumina-supported ruthenium and generated electron deficient ruthenium species. besides increasing their interaction with the support. The addition of magnesium increased the ruthenium dispersion but did not increase the methane conversion, suggesting that it negatively changed the electron properties of ruthenium towards methane conversion. However, it avoided deactivation during reaction and changed the activity for the water gas shift reaction, allowing tailoring the hydrogen to carbon monoxide molar ratio, The catalysts showed activity close or higher than a commercial sample, indicating that they are promising for the reaction, with the advantage that it can be tailored for several applications. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:52 / 60
页数:9
相关论文
共 43 条
[1]   Preparation and characterization of MgO/Al2O3 mixed oxides support for hydrotreating catalysts [J].
Aberuagba, F ;
Kumar, M ;
Gupta, JK ;
Muralidhar, G ;
Sharma, LD .
REACTION KINETICS AND CATALYSIS LETTERS, 2002, 75 (02) :245-250
[2]   Effect of ageing on a steam reforming catalyst [J].
alQahtani, H .
CHEMICAL ENGINEERING JOURNAL, 1997, 66 (01) :51-56
[3]   Kinetics of steam reforming of methane on Ru/Al2O3 catalyst promoted with Mn oxides [J].
Berman, A ;
Karn, RK ;
Epstein, A .
APPLIED CATALYSIS A-GENERAL, 2005, 282 (1-2) :73-83
[4]   A study of the ruthenium-alumina system [J].
Betancourt, P ;
Rives, A ;
Hubaut, R ;
Scott, CE ;
Goldwasser, J .
APPLIED CATALYSIS A-GENERAL, 1998, 170 (02) :307-314
[5]   Catalytic steam reforming of methane over La0.8Sr0.2CrO3 based Ru catalysts [J].
Caillot, T. ;
Gelin, P. ;
Dailly, J. ;
Gauthier, G. ;
Cayron, C. ;
Laurencin, J. .
CATALYSIS TODAY, 2007, 128 (3-4) :264-268
[6]   Controlled preparation and characterization of plurimetallic Pt-Sn and Pt-Ir-Sn/Al2O3 reforming catalysts [J].
Carnevillier, C ;
Epron, F ;
Marecot, P .
APPLIED CATALYSIS A-GENERAL, 2004, 275 (1-2) :25-33
[7]  
CROSS JRH, 1996, CATAL TODAY, V30, P193
[8]   Catalytic evaluation of perovskite-type oxide LaNi1-xRuxO3 in methane dry reforming [J].
de Arauj, Genira Carneiro ;
de Lima, Sania Maria ;
Assaf, Jose Mansur ;
Pena, Miguel Antonio ;
Garcia Fierro, Jose Luis ;
Rangel, Maria do Carmo .
CATALYSIS TODAY, 2008, 133 (129-135) :129-135
[9]  
DRY ME, 1984, CATALYSIS SCI TECHNO, V1, P106
[10]   A dynamic study of steam-methane reforming [J].
El-Bousiffi, M. A. ;
Gunn, D. J. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2007, 50 (3-4) :723-733