Slurry-phase
hydrocracking of vacuum residue using a dispersed
catalyst has been investigated in this work. The liquid yield and
coke formation in this process mostly depend upon the catalyst particle
size and its distribution. Three emulsion methods, colloidal emulsion
liquid (CEL), emulsion liquid membrane (ELM), and reverse micelle
(RM), are used to synthesize the dispersed MoS2 catalyst.
Dynamic light scattering results show that the colloidal particle
of molybdenum sulfide in the RM catalyst is smaller in size and narrowly
distributed in comparison to the catalysts prepared by CEL and ELM
methods. Our scanning electron microscopy and transmission electron
microscopy analysis results also support the smaller particle size
of the active metal in the RM catalyst. Hydrotreating and hydrocracking
activities of the RM catalyst are higher, and it is due to its smaller
particle size and its narrow distribution. Moreover, coke formation
in this catalyst is very low. It is found that the residue (550 °C+
hydrocarbons) is mostly converted into the middle distillates and
vacuum gas oil by this catalyst. A lower mole percentage of unconsumed
hydrogen in the gaseous product and higher hydrogen/carbon ratio in
the liquid product also indicate the higher hydrogenation activity
of the RM catalyst. The total liquid yield in this catalyst is also
higher, suggesting the deep hydrocracking of the large hydrocarbons.
Therefore, the RM emulsion is a suitable method to prepare the residue
hydrocracking catalyst with proper morphology.