Bio-oil upgrading over platinum catalysts using in situ generated hydrogen

Abstract The liquid phase upgrading of a model bio-oil was studied over a series of supported Pt catalysts. Pt/Al 2 O 3 showed the highest activity for deoxygenation, the oxygen content of the model oil decreasing from an initial value of 41.4 wt% to 2.8 wt% after upgrading. GC–MS analysis of the oil showed it to be highly aromatic, the major components corresponding to alkyl-substituted benzenes and cyclohexanes. CO 2 was formed as the major gaseous product, together with lower yields of H 2 and C 1 –C 6 hydrocarbons. Based on the product distribution, a reaction scheme is proposed in which light oxygenates predominantly undergo reforming to CO 2 and H 2 , with C–O bond breaking/hydrogenation (to afford alkanes) as a minor pathway. In a parallel process, aromatics undergo C–O cleavage/hydrogenation, affording benzenes and cyclohexanes. The highly alkylated nature of the products appears to be a consequence of the acidic nature of the reaction medium, favoring the occurrence of aromatic electrophilic substitution reactions.

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