Performance of catalysts with Nb2O5 for hydrogen production from ethanol steam reforming

• Autor(a) principal: Machado, Nádia Regina Camardo Fernandes
• Data de Publicação: 2008
• Outros Autores: Rizzo, Roberta Carolina Pelissari, Peguin, Robson Pablo Sobradiel
• Tipo de documento: Artigo
• Idioma: por
• Título da fonte: Acta scientiarum. Technology (Online)
• Texto Completo: http://www.periodicos.uem.br/ojs/index.php/ActaSciTechnol/article/view/2484
• topic: reforma de etanol com vapor d’água; produção de hidrogênio; catalisadores Cu/Nb2O5; 3.06.00.00-6 Engenharia Química

Cu/Nb2O5 and Cu/Nb2O5/Al2O3 were studied as catalysts in ethanol steam-reforming for hydrogen production. They were prepared through impregnation, with different copper and Nb2O5 concentrations. Cu/ZnO/Al2O3 (G66), a commercial catalyst for methanol reforming was used for comparison. Temperature-programmed reduction data showed incomplete reduction of the copper, resulting in two reduction peaks, in opposition to CuO bulk, whose reduction occurred in one step (only one peak), it evidences a copper modification through Nb2O5. Results of diffuse reflectance spectra also evidenced the interaction. The catalytic tests showed that the niobium oxide dispersion on alumina improved the catalyst action; the ternary catalysts are the ones that show higher hydrogen production. They also produce ethyl ether as side product. The binary catalysts don't present parallel reaction, probably because when Cu/Nb2O5 is dispersed on alumina there is another type of catalytic site production, which produces ethyl ether.