In
this study, we report a single-step continuous production of
straight-chain liquid hydrocarbons from oleic acid and other fatty
acid derivatives of interest including castor oil, frying oil, and
palm oil using Mo, MgO, and Ni on Al
2
O
3
as catalysts
in subcritical water. Straight-chain hydrocarbons were obtained via
decarboxylation and hydrogenation reactions with no added hydrogen.
Mo/Al
2
O
3
catalyst was found to exhibit a higher
degree of decarboxylation (92%) and liquid yield (71%) compared to
the other two examined catalysts (MgO/Al
2
O
3
,
Ni/Al
2
O
3
) at the maximized conditions of 375
°C, 4 h of space time, and a volume ratio of 5:1 of water to
oleic acid. The obtained liquid product has a similar density (0.85
kg/m
3
at 15.6 °C) and high heating value (44.7 MJ/kg)
as commercial fuels including kerosene (0.78–0.82 kg/m
3
and 46.2 MJ/kg), jet fuel (0.78–0.84 kg/m
3
and 43.5 MJ/kg), and diesel fuel (0.80–0.96 kg/m
3
and 44.8 MJ/kg). The reaction conditions including temperature,
volume ratio of water-to-feed, and space time were maximized for the
Mo/Al
2
O
3
catalyst. Characterization of the spent
catalysts showed that a significant amount of amorphous carbon deposited
on the catalyst could be removed by simple carbon burning in air with
the catalyst recycled and reused.