Abstract
A series of NiMo catalysts with a low MoO3/NiO mass ratio were prepared by introducing SiO2 and Ni during the formation of the support. The supports were improved by adding SiO2 to optimise the surface acidity properties, regulate the main structure of the NiMoS active phase, reduce the formation proportion of NiAl2O4, and improve the utilisation rate of Ni. The catalysts were improved by increasing the Ni content to adjust the Ni/Mo atomic ratio at the edge and corner positions of the NiMoS active phase to promote the generation and transfer of activated hydrogen. The NiMoS phase with high Ni content achieved good dispersion on the catalyst surface, reaching the highest hydrogenation saturation depth of aromatic hydrocarbon when the MoO3/NiO mass ratio is 3 and the SiO2 content is 5 wt.%. The catalysts with high Ni content also exhibit high activity and stability in removing Conradson Carbon Residue (CCR) during hydrotreating. Increasing the Ni content of the catalyst helps to remove impurities such as S and N from the residual oil.