Fluid catalytic cracking (FCC) gasolines are the most
important
components of blend gasolines. They are characterized by high octane
number due to the great amount of olefins in their composition. However,
one of the problems concerning FCC gasolines is the necessity of selective
removal of diolefins, which can cause deactivation of catalysts for
FCC gasoline hydrofining. In spite of the fact that NiMo/γ-Al2O3 catalysts are usually used in the industrial
process of selective diene hydrogenation, literature data on the influence
of NiMo catalyst composition on the catalytic performance in selective
diolefins hydrogenation are poorly covered. Therefore, the main goal
of the present work was to clarify the aspects of the effect of NiMo/γ-Al2O3 catalyst composition on their catalytic properties.
The main feature of the catalysts was the higher Ni/Mo molar ratio
(0.5 to 2) compared to those for the hydrotreating catalysts. The
impregnating solutions, the support, and the catalysts were studied
by nitrogen adsorption–desorption, attenuated total reflection
Fourier transform infrared spectroscopy, Raman spectroscopy, UV–vis
diffuse reflectance spectroscopy, X-ray diffraction, high-resolution
transmission electron microscopy, and X-ray photoelectron spectra.
It was found that the increase in the Ni/Mo molar ratio from 0.5 to
2 resulted in the formation of the mixture of complex compounds like
Ni–citrate, Mo–citrate, and NiMo–citrate complexes.
It further influences the formation of the sulfide active component;
especially, there is a decrease in the interaction of active metals
with the support due to implementation of Ni to the support structure.
It was found that the excess nickel in the catalysts also contributed
to the greater promotion of MoS2 particles and the formation
of bulk nickel sulfide particles. It was shown that the higher the
Ni/Mo molar ratio, the higher the activity in selective isoprene hydrogenation,
while selectivity did not depend on the molar ratio of active metals.
The highest activity in isoprene hydrogenation was obtained for Ni/Mo
molar ratio = 2.