Method used for preparing hydrogenation catalyst

Abstract

The invention discloses a method used for preparing a hydrogenation catalyst. The method comprises steps of preparation of an aluminium oxide-based carrier containing silicon and magnesium, and loading of a hydrogenation active metal; in the step of preparation of the aluminium oxide-based carrier containing silicon and magnesium, water soluble silicone oil and a soluble magnesium-containing compound are introduced into an aluminium oxide-based carrier successively or simultaneously, and the aluminium oxide-based carrier containing silicon and magnesium is obtained via heat treatment. The method is capable of adjusting distribution of acid centers and hydrogenation active centers, achieving coordination effects, and improving comprehensive performance of the hydrogenation catalyst.

Description

technical field [0001] The invention relates to a method for preparing a hydrogenation treatment catalyst, in particular to a preparation method suitable for a heavy distillate oil hydrogenation treatment catalyst. Background technique [0002] Most supported catalysts are prepared by impregnation method, such as various hydrogenation catalysts. Alumina is often used as a carrier material for this type of catalyst. but pure Al 2 o 3 The interaction force between the active metal on the surface and the carrier is relatively large, and it is easy to form inactive species (such as the formation of nickel-aluminum spinel), and it is difficult to completely vulcanize to form a type II active phase with high hydrogenation activity. At the same time, the acidity of the catalyst surface has a great influence on the activity of the hydrogenation catalyst. The removal of heteroatoms in the raw material requires the catalyst to have hydrogenolysis activity, which occurs on the acidi...

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Problems solved by technology

[0006] The above-mentioned prior art uses co-precipitation method or adding additives during molding. The former will cause active metals and Si and other additives to enter the bulk phase during the co-precipitation process, and multiple substances are precipitated at the same time. The same precipitation conditions cannot be simultaneously The best precipitation conditions for a variety of substances, and the additives have no selectivity to the formation of the active metal active phase and the adjustment of the acidity of the catalyst, thus affecting the overall performance of the final catalyst; while the latter adds Si and other additives during kneading molding, It is not conducive to the uniform dispersion of additives, not only the utilization rate of additives is reduced, but also the comprehensive adjustment effect on the acidity and activity of the catalyst is weak, which is not conducive to the improvement of the comprehensive performance of the catalyst