CPC C10G 49/04 (2013.01) [B01J 23/883 (2013.01); B01J 35/1009 (2013.01); B01J 35/1014 (2013.01); B01J 35/1019 (2013.01); B01J 35/1038 (2013.01); B01J 35/1042 (2013.01); B01J 35/1047 (2013.01); B01J 37/0205 (2013.01); B01J 37/088 (2013.01)] | 5 Claims |
1. A hydrogenolysis process wherein a hydrocarbon-based feedstock comprising aromatic compounds having at least 8 carbon atoms is treated by means of an introduction of hydrogen and in the presence of a catalyst, to convert C2+ alkyl chains of said aromatic compounds into methyl groups and to produce a hydrogenolysis effluent enriched in methyl-substituted aromatic compounds,
wherein the hydrogenolysis process is carried out with the following operating conditions:
temperature of between 300° C. and 550° C.;
pressure of between 0.1 and 3 MPa;
H2/HC molar ratio of between 1 and 10;
WWH of between 0.1 and 50 h−1, and
wherein the catalyst comprises a support comprising at least one refractory oxide, and an active phase comprising nickel and molybdenum, wherein:
the nickel content is between 0.1 and 25% by weight relative to the total weight of the catalyst;
the molybdenum content is between 0.1 and 20% by weight relative to the total weight of the catalyst; and
the catalyst comprises a molar ratio of molybdenum to nickel (Mo/Ni) of between 0.2 and 0.9.
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