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Hydrodeoxygenation of phenol and biomass fast pyrolysis oil (bio-oil) over Ni/WO3-ZrO2 catalyst

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Abstract The hydrodeoxygenation of pure phenol in hexane solution and of catalytic biomass fast pyrolysis oil (bio-oil) over 10%Ni/ZrO2 and 10%Ni/WO3-ZrO2 catalysts was investigated in the present study, at relatively… Click to show full abstract

Abstract The hydrodeoxygenation of pure phenol in hexane solution and of catalytic biomass fast pyrolysis oil (bio-oil) over 10%Ni/ZrO2 and 10%Ni/WO3-ZrO2 catalysts was investigated in the present study, at relatively mild conditions (ca. 50-250 °C, 30 bar H2) in a continuous flow high-pressure fixed bed reactor. The catalysts were characterized for their structural, porosity, redox and acidic/basic properties which were used to rationalize the observed catalytic performance. The 10%Ni/ZrO2 catalyst was very active and selective towards cyclohexanol in the phenol HDO experiments (100% conversion and selectivity at 110 °C) but the enhanced acidity offered by the addition WO3 in ZrO2 was necessary to succeed a complete hydrodeoxygenation of phenol to cyclohexane at the low temperature of 150 °C with the 10%Ni/WO3-ZrO2 catalyst. This catalyst was also proven very active in the hydrodeoxygenation of the catalytic bio-oil which consisted of mono-aromatics (i.e. alkyl-benzenes) and PAHs (mainly naphthalenes and indenes), and fewer oxygenated compounds (i.e. alkyl-phenols and benzofurans), providing a product oil containing mainly alkyl-cycloalkanes and fewer alkyl-benzenes, at the mild conditions of 210 °C and 30 bar H2.

Keywords: zro2; wo3 zro2; catalyst; hydrodeoxygenation; oil

Journal Title: Catalysis Today
Year Published: 2020

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