This
study investigates the promotional effects of a potentially
new class of oil-soluble dispersed catalyst precursors for upgrading
of vacuum gas oil (VGO), that is metal-based p-tert-butylcalix[4]arenes (TBC[4]s). Co- and Ni-TBC[4] were
synthesized, and the metal–ligand complexation was confirmed
by scanning electron microscopy-energy dispersive X-ray, inductively
coupled plasma, X-ray diffraction, UV–vis, Fourier transform
infrared, and 1H NMR. The thermogravimetric and calorimetric
behaviors of the synthesized complexes, which are key properties of
dispersed hydrocracking catalysts, were also studied. The differential
scanning calorimetry profile of Ni-TBC[4] and Co-TBC[4] showed that
the organometallic structure has lower thermal stability compared
with that of the parent TBC[4]. This apparent drawback can be positively
exploited by employing TBC[4] as a carrier of the metal, where the
active sites are formed in situ by the destruction of the organometallic
complex on reaching the desired reaction conditions. The catalytic
performance of the synthesized precursors was evaluated using a batch
autoclave reactor with varying concentrations of catalyst precursors
at 420–450 °C. The results show that the synthesized metal-based
TBC[4] dispersed catalysts evidently enhanced the hydrogenation activity
and reduced coke formation. The addition of 500 ppm Co and Ni as standalone
dispersed catalysts produced distillate yields of 45.7 and 49.7 wt
% and a coke laydown of 2.6 and 2.3 wt %, respectively. Increasing
the concentration of catalyst precursors enhanced the conversion of
VGO from 86.17% at 100 ppm Ni to 88.28% at 500 ppm Ni. Moreover, as
the metal concentration increased from 100 to 500 ppm, the distillate
yield increased from 36.87 to 49.66 wt %, while the yield of gases
decreased from 20.48 to 17.12 wt % because the hydrogenation reactions
were enhanced. In contrast, the yields of distillate and naphtha decreased
by 14.12 and 15.36%, respectively, as the temperature increased from
420 to 450 °C.