发明名称 PROCESS FOR THE HYDRODESULPHURIZATION OF HYDROCARBON CUTS
摘要 A process for the concomitant production of at least two hydrocarbon cuts with low sulphur contents from a mixture of hydrocarbons having a total sulphur content in the range 30 to 10000 ppm by weight, by a) hydrodesulphurization in the presence of hydrogen and a hydrodesulphurization catalyst;b) separating hydrogen sulphide from the partially desulphurized effluent obtained from a);c) hydrodesulphurization of the partially desulphurized mixture obtained from b) in the presence of hydrogen and a hydrodesulphurization catalyst, the temperature of the second hydrodesulphurization being higher than that of the first hydrodesulphurization;d) fractionating the desulphurized mixture obtained in c) into at least two desulphurized hydrocarbon cuts.
申请公布号 US2015166907(A1) 申请公布日期 2015.06.18
申请号 US201414572946 申请日期 2014.12.17
申请人 IFP ENERGIES NOUVELLES 发明人 GORNAY Julien;LEFLAIVE Philibert;TOUZALIN Olivier;PUCCI Annick;LARGETEAU Delphine
分类号 C10G67/02 主分类号 C10G67/02
代理机构 代理人
主权项 1. A process for the concomitant production of at least two hydrocarbon cuts with low sulphur contents from a mixture of hydrocarbons having an initial boiling temperature in the range 35° C. to 100° C. and a final boiling temperature in the range 260° C. to 340° C. and having a total sulphur content in the range 30 to 10000 ppm by weight, said hydrocarbon mixture comprising: at least one first fraction comprising hydrocarbons having a boiling temperature range in the range from the initial boiling temperature of the mixture to 160° C. and with an olefins content in the range 20% to 80% by weight of said first fraction; and at least one second fraction comprising hydrocarbons having a boiling temperature range in the range 160° C. to the final boiling temperature of the mixture, said second fraction comprising at least 10% by weight of hydrocarbons with a boiling temperature range in the range 220° C. to the final boiling temperature of the mixture;the process comprising the following steps:a) in a first reactor, treating the mixture in a first hydrodesulphurization step in the presence of hydrogen and a catalyst comprising at least one metal from group VIII, at least one metal from group VIB and a support, the first hydrodesulphurization step being carried out at a temperature in the range 200° C. to 400° C., at a pressure in the range 1 to 10 MPa, with a liquid hourly space velocity in the range 0.1 to 10 h−1 and with a (volume of hydrogen/volume of hydrocarbon mixture) ratio in the range 50 to 500 Nlitre/litre;b) separating at least a portion of the hydrogen sulphide from the partially desulphurized effluent obtained from step a);c) in a second reactor, treating the partially desulphurized mixture obtained from step b) in a second hydrodesulphurization step in the presence of hydrogen and a catalyst comprising at least one element from group VIII, at least one element from group VIB and a support, the second hydrodesulphurization step being carried out at a temperature in the range 205° C. to 500° C., at a pressure in the range 1 to 3 MPa, with a liquid hourly space velocity in the range 1 to 10 h−1 and with a (volume of hydrogen/volume of mixture) ratio in the range 50 to 50 Nlitre/litre, the temperature of the second hydrodesulphurization step c) being higher than that of the first hydrodesulphurization step a); andd) fractionating the desulphurized mixture obtained from step c) into at least two desulphurized hydrocarbon cuts, light and heavy, the light hydrocarbon cut having an initial boiling temperature in the range 35° C. to 100° C. and a final boiling temperature in the range 160° C. to 220° C. and wherein the total sulphur content is less than 50 ppm by weight and the heavy hydrocarbon cut has an initial boiling temperature in the range 160° C. to 220° C. and a final boiling temperature in the range 260° C. to 340° C.
地址 RUEIL-MALMAISON CEDEX FR
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