Production of CH by methanation of biogas provides a promising route towards sustainable energy production for the future. Utilization of biogas from biomass as CO source combines the advantage of reduction of greenhouse gas emissions producing a fuel with high energy density. In this study we apply a dip-spin coating method for washcoating Ni(7.5 wt%)Rh(0.5 wt%)/CeO catalyst on alumina open cell foams with different cell densities (20, 30 and 40 PPI). The catalytic activity of the structured samples was assessed using a gas mixture that simulates a typical biogas composition (CH = 60%vol; CO = 40%vol). The effects of the reaction temperature (300-600 °C) and H/CO molar ratio in the feed (3-5) on the CO conversion and CH selectivity were evaluated under a gas hourly space velocity (GHSV) of 5100 h. All samples showed appreciable CO conversion ranging between 62.5 and 66.7% at reaction temperature of 500-600 °C, and a CH productivity of 3.4 mol·g·h was obtained with the catalyst supported on open cell foam with 30 and 20 PPI under a reaction temperature of 400 °C.
RhNi/CeO2 catalytic activation of alumina open cell foams by dip-spin coating for the CO2 methanation of biogas
Drago Ferrante G;Italiano C;Vita A;Pino L
2022
Abstract
Production of CH by methanation of biogas provides a promising route towards sustainable energy production for the future. Utilization of biogas from biomass as CO source combines the advantage of reduction of greenhouse gas emissions producing a fuel with high energy density. In this study we apply a dip-spin coating method for washcoating Ni(7.5 wt%)Rh(0.5 wt%)/CeO catalyst on alumina open cell foams with different cell densities (20, 30 and 40 PPI). The catalytic activity of the structured samples was assessed using a gas mixture that simulates a typical biogas composition (CH = 60%vol; CO = 40%vol). The effects of the reaction temperature (300-600 °C) and H/CO molar ratio in the feed (3-5) on the CO conversion and CH selectivity were evaluated under a gas hourly space velocity (GHSV) of 5100 h. All samples showed appreciable CO conversion ranging between 62.5 and 66.7% at reaction temperature of 500-600 °C, and a CH productivity of 3.4 mol·g·h was obtained with the catalyst supported on open cell foam with 30 and 20 PPI under a reaction temperature of 400 °C.I documenti in IRIS sono protetti da copyright e tutti i diritti sono riservati, salvo diversa indicazione.
