Method for hydrodesulfurization in the presence of a catalyst on a mesoporous-macroporous substrate
AssigneeIfp Energies Nouvelles
InventorsPhilibert Leflaive, Etienne Girard, Antoine Fecant
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AssigneeIfp Energies Nouvelles
InventorsPhilibert Leflaive, Etienne Girard, Antoine Fecant
Estimating the term…
For hydrodesulfurization of an olefinic gasoline cut containing sulfur, the gasoline cut, hydrogen, and a catalyst are brought into contact. The catalyst comprises a group VIB metal, a group VIII metal, and a mesoporous and macroporous alumina substrate having a bimodal mesopore distribution. The volume of mesopores having a diameter greater than or equal to 2 nm and less than 18 nm corresponds to between 10 and 30% by volume of the total pore volume of the substrate. The volume of mesopores having a diameter greater than or equal to 18 nm and less than 50 nm corresponds to between 30 and 50% by volume of the total pore volume of the substrate. The volume of macropores having a diameter greater than or equal to 50 nm and less than 8000 nm corresponds to between 30 and 50% by volume of the total pore volume of the substrate.
A process for hydrodesulfurization of an olefinic gasoline cut containing sulfur, wherein said olefinic gasoline cut, hydrogen and a catalyst are brought into contact, said hydrodesulfurization process being carried out at a temperature of between 200° C. and 400° C., a total pressure of between 1 and 3 MPa, an hourly space velocity, defined as being the volume flow rate of feedstock relative to the volume of catalyst, of between 1 and 10 h−1 and a hydrogen/olefinic gasoline cut volume ratio of between 100 and 600 N1/1, said catalyst comprising at least one group VIB metal, at least one group VIII metal, and a mesoporous and macroporous alumina support comprising a bimodal distribution of mesopores and wherein:
Dependencies are inferred from the claim text.