This work demonstrated an effective approach to upgrading
bio-oils
by upgrading pyrolysis bio-oil with vacuum gas oil (VGO) by catalytic
hydrodeoxygenation (HDO) in supercritical ethanol with both hydrogen
gas and formic acid as the in situ hydrogen source.
The effects of supercritical ethanol, bio-oil/VGO mass ratio, reaction
temperature, hydrogen source, and reaction time on co-upgrading pyrolysis
bio-oil with VGO over Ru/Al2O3 were investigated
in this study. Crude bio-oil, crude VGO, and co-upgraded oils were
characterized comparatively for their physical/chemical properties
and compositions. It was found that the optimal reaction conditions
of co-upgrading bio-oil with VGO were at a 4:1 mass ratio, in supercritical
ethanol, with hydrogen gas as the hydrogen source, and at 350 °C
for 2 h over the Ru/Al2O3 catalyst. The obtained
co-upgraded oils have improved thermal stability and homogeneity,
which could be used as an environmentally friendly and sustainable
feed for large-scale upgrading in a petroleum refinery.