Abstract
In this article, I want to introduce new methods for calculating the hydrodesulfurization process of diesel fuel.
 Mathematical models for the interpretation of the feed stock and reaction rate constants for multicomponent systems are considered. Taking into account these models, the operation of industrial reactor blocks of hydrotreatment units is analyzed and new options for their prospective implementation are presented. It has been shown that these options will make it possible to reduce the amount of catalyst in the reactors.
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