Produção de hidrogênio a partir da reforma a vapor de etanol utilizando catalisadores Cu/Ni/γ-Al2O3

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Abstract

Cu/Ni/γ-Al2O3 catalysts were prepared by an impregnation method with 2.5 or 5% wt of copper and 5 or 15% wt of nickel and applied in ethanol steam reforming. The catalysts were characterized by atomic absorption spectrophotometry, X-ray diffraction, temperature programmed reduction with hydrogen and nitrogen adsorption. The samples showed low crystallinity, with the presence of CuO and NiO, both as crystallites and in dispersed phase, as well as of NiO-Al2O3. The catalytic tests carried out at 400°C, with a 3:1 water/ethanol molar ratio, indicated the 5Cu/5Ni/Al2O3 catalyst as the most active for hydrogen production, with a hydrogen yield of 77% and ethanol conversion of 98%.

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Maia, T. A., Bellido, J. D. A., Assaf, E. M., & Assaf, J. M. (2007). Produção de hidrogênio a partir da reforma a vapor de etanol utilizando catalisadores Cu/Ni/γ-Al2O3. Quimica Nova, 30(2), 339–345. https://doi.org/10.1590/S0100-40422007000200019

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