Abstract

The catalytic conversion of model compounds (e.g. cyclopentanone, cyclopentenone, furfural, glycerol, glucose, fructose and their derivatives usually found in the pyrolysis oils of biomass materials) to hydrocarbon products over H-ZSM-5, Zn-ZSM-5 and Mn-ZSM-5 zeolite catalysts have been studied in a fixed bed microreactor at temperatures ranging from 350°C to 500°C. Although the deoxygenation of cyclopentanone was completed at 400°C, low yields of hydrocarbons were obtained for furfural, glycerol and carbohydrate derivatives. This is due possibly to thermal polymerization at reaction temperatures of 400°C and higher. Increasing the (H/C)eff ratio of the feed with methanol increased significantly the hydrocarbon yield of furfural but not that of carbohydrates. Reaction mechanisms for deoxygenation and tar formation are proposed.

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