CPC C10G 45/06 (2013.01) [B01J 21/04 (2013.01); B01J 23/755 (2013.01); B01J 35/50 (2024.01); B01J 35/613 (2024.01); B01J 35/615 (2024.01); B01J 35/635 (2024.01); B01J 35/638 (2024.01); B01J 35/647 (2024.01); B01J 35/651 (2024.01); B01J 35/653 (2024.01); B01J 35/657 (2024.01); B01J 35/69 (2024.01); B01J 37/0205 (2013.01); B01J 37/088 (2013.01); C10G 2300/202 (2013.01); C10G 2400/02 (2013.01)] | 17 Claims |
1. A process for treating a partially desulfurized, sulfur-containing hydrocarbon feedstock resulting from a preliminary step of catalytic hydrodesulfurization, said process comprising:
subjecting said feedstock to partially desulfurization at a temperature of between 200° C. and 400° C., a pressure of between 0.2 and 5 MPa, at an hourly space velocity, defined as the volume flow rate of feedstock at the inlet per volume of catalyst used, of between 0.1 h−1 and 20 h−1, in the presence of a catalyst comprising an active phase comprising at least one group VIII metal, said active phase not comprising any group VIB metal, and a mesoporous and macroporous alumina support comprising a bimodal distribution of mesopores and wherein:
the volume of mesopores with 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 said support;
the volume of mesopores with 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 said support;
the volume of macropores with 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 said support.
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