In
this work, deep extractive catalytic oxidative desulfurization
(ODS) of hydrotreated real diesel fuel was attained using a synthesized
catalyst of supported molybdenum oxide on mesoporous silica gel (MoO3/SG) with a high surface area. The characterization of the
catalyst was assessed by Fourier transform infrared, X-ray diffraction,
Brunauer–Emmett–Teller, Barrett–Joyner–Halenda,
N2 adsorption–desorption, scanning electron microscopy,
and energy-dispersive X-ray spectroscopy analysis. The effect of molybdenum loading, M
catalyst/V
oil, H2O2/sulfur
molar ratio, temperature, and reaction duration on the ODS of diesel
was examined, aiming to set at the optimum values. Different extraction
solvents were evaluated, where acetonitrile was processed with the
best performance among all. About 99.9% of sulfur in real diesel was
selectively removed using the MoO3 (5 wt %)/SG catalyst
under the optimal mild reaction conditions of 45 °C, an O/S molar
ratio of 8, an M
catalyst/V
oil of 0.1 g/mL, and a reaction time of 90 min, employing
only one step extraction of ODS products by acetonitrile. Compared
to previous research studies on ODS of real diesel, an obviously superior
performance was exhibited by the introduced catalyst in this study
because of the sufficiently large pore diameter, considerably higher
surface area (346.5 m2/g) of the catalyst, good distribution
of the active phase on the SG surface, and ODS operating at the optimal
conditions. Interestingly, no significant loss in catalyst activity
was revealed after recycling seven times in ODS of the dibenzothiophene
model; however, the catalyst reusability was relatively limited by
the interactions of various hydrocarbons in the real diesel. The studies
on overall kinetics and reaction pathway were conducted as well.