Abstract
In the present work, ethanol has been selected as a model compound to represent the typical alcohols found in bio-oil. A stable Ni/CeO2 catalyst has been designed for the production of hydrogen from catalytic steam reforming of ethanol in a continuous-flow fixed-bed reactor. The influence of reaction temperature, liquid hourly space velocity, and steam-to-carbon ratio were investigated. The Ni/CeO2 catalyst performed with high activity for 30 h at optimal conditions and did not show any deactivation. Using density functional theory, the elementary reactions involved in the decomposition of ethanol on the Ni(111) surface have been systematically calculated. The optimal pathway for the ethanol steam reforming reaction process on the surface of the catalyst is proposed.