LAUSR

Abstract This article presents the findings of our research regarding the supercritical water gasification of a real biomass, olive mill wastewater, with Ni/Al 2 O 3 and Ru/Al 2 O 3 catalysts. The experiments were performed at five reaction temperatures between 400 and 600 °C, for five reaction times ranging from 30 to 150 s and at a constant pressure of 25 MPa. It was seen that the employment of catalysts enhanced the gasification and biofuel production yield, which mainly involved methane and hydrogen. Ni/Al 2 O 3 was selective for hydrogen formation, whereas Ru/Al 2 O 3 favored the formation of methane. The highest calorific value of the produced biofuel was obtained as 56123 kJ/m 3 with Ru/Al 2 O 3 at 600 °C and 60 s. Apart from biofuel production, the simultaneous treatment of the wastewater was also accomplished. At elevated temperatures and times, treatment efficiencies greater than 97% based on total organic carbon conversion were reached. Moreover, the kinetic evaluation of the catalytic supercritical water gasification of olive mill wastewater was performed based on first order reaction kinetics.