INCAPE   05401
INSTITUTO DE INVESTIGACIONES EN CATALISIS Y PETROQUIMICA "ING. JOSE MIGUEL PARERA"
Unidad Ejecutora - UE
artículos
Título:
Supported Rh nanoparticles on CaO-SiO2 bynary systems for the reforming of methane by carbon dioxide in membrane reactors
Autor/es:
J. MÚNERA; B. FAROLDI; E. FRUTIS; E. LOMBARDO; L. CORNAGLIA; S. GONZALEZ CARRAZÁN
Revista:
APPLIED CATALYSIS A-GENERAL
Editorial:
ELSEVIER SCIENCE BV
Referencias:
Lugar: Amsterdam; Año: 2014 vol. 474 p. 114 - 124
ISSN:
0926-860X
Resumen:
A set of Rh catalysts supported on binary CaO-SiO2 system with different CaO content were prepared. The textural and structural properties, Rh particle size, and catalytic performance in the dry reforming of methane reaction were investigated. The Rh nanoparticles and nanocrystalline structures in the reduced catalysts were characterized through HRTEM and CO chemisorption. EDX mapping showed that CaO is uniformly distributed on SiO2 and no segregation is detected between them. Rh nanoparticles of about 1-2.6 nm were observed. These particles sizes indicate that Rh is well dispersed on the catalyst surface and that no agglomeration exists. The incorporation of the promoter (CaO) to the silica support induces an increase in the metal dispersion, however the Rh dispersion decreased when the CaO loading is increased. For the high CaO load solids, a high stability was observed after 80 hours on stream for the dry reforming of methane. In addition, the solid with 27% CaO presented the higher methane reaction rate. As a consequence, this solid was selected for its application in a membrane reactor under different conditions. The increase of methane conversion with reaction pressure at high sweep gas flow rate indicates that the separation efficiency of the Pd membrane is sufficiently high to dominate the performance of Pd membrane reactors under those conditions.