Process for the hydrodesulphurization of hydrocarbon cuts

Patent metadata

Field	Value
Publication number	US-9505993-B2
Application number	US-201414572946-A
Country	US
Kind code	B2
Filing date	Dec 17, 2014
Priority date	Dec 18, 2013
Publication date	Nov 29, 2016
Grant date	Nov 29, 2016

Abstract

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.

First claim

The invention claimed is:

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 Nliter/liter;
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 500 Nliter/liter, the temperature of the second hydrodesulphurization step c) being higher than that of the first hydrodesulphurization step a); and
d) 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.

2. The process according to claim 1 , in which the catalyst for step a) comprises a metal from group VIII selected from nickel and cobalt and a metal from group VI selected from molybdenum and tungsten.

3. The process according to claim 1 , in which the catalyst for step a) comprises phosphorus.

4. The process according to claim 1 , in which the catalyst for step c) comprises a metal from group VIII selected from nickel and cobalt and a metal from group VI selected from molybdenum and tungsten.

5. The process according to claim 4 , in which the catalyst for step c) further comprises phosphorus.

6. The process according to claim 1 , in which the first hydrocarbon fraction is a gasoline cut obtained from a catalytic cracking unit.

7. The process according to claim 6 , in which the first hydrocarbon fraction is a C6 + hydrocarbon cut obtained by distillation of a gasoline cut obtained from a catalytic cracking unit.

8. The process according to claim 7 in which, before the distillation step, the gasoline cut has undergone a step for selective hydrogenation of the diolefins present in said gasoline cut.

9. The process according to claim 6 in which, before step a), a step is carried out for mixing the first and second hydrocarbon cuts upstream of the reactor for the first hydrodesulphurization step.

10. The process according to claim 6 , in which the first and second hydrocarbon cuts are mixed in the reactor for the first hydrodesulphurization step.

11. The process according to claim 1 , in which the second hydrocarbon fraction is selected from a light cycle oil, a heavy diesel cut, a vacuum distillate cut, a hydrocarbon cut obtained from a visbreaking unit and a hydrocarbon cut obtained from a coking unit.

12. The process according to claim 1 , in which the mixture contains a gasoline cut and a light cycle oil.

13. The process according to claim 12 , in which said mixture is the product of a distillation of an effluent obtained from a catalytic cracking unit.

14. The process according to claim 1 , in which the temperature of step c) is higher than the temperature of step a) by at least 5° C.

15. The process according to claim 1 , in which the temperature of step c) is higher than the temperature of step a) by at least 10° C.

Assignees

• Ifp Energies Now

Inventors

• Gornay Julien
• Leflaive Philibert
• Touzalin Olivier
• Pucci Annick
• Largeteau Delphine

Classifications

• C10G45/04 Primary

  characterised by the catalyst used · CPC title

• C10G2400/04

  Diesel oil · CPC title

• C10G65/04

  including only refining steps · CPC title

• C10G2300/1055

  Diesel having a boiling range of about 230 - 330 °C · CPC title

• C10G2400/02

  Gasoline · CPC title