Conversion process comprising at least one step for fixed bed hydrotreatment and a step for hydrocracking in by-passable reactors

Patent metadata

Field	Value
Publication number	US-10266779-B2
Application number	US-201715616418-A
Country	US
Kind code	B2
Filing date	Jun 7, 2017
Priority date	Jun 9, 2016
Publication date	Apr 23, 2019
Grant date	Apr 23, 2019

Abstract

The invention concerns a process for the treatment of a hydrocarbon feed in order to obtain a heavy hydrocarbon fraction with a low sulphur content, said process comprising the following steps: a) an optional step for hydrodemetallization carried out in permutable reactors, b) a step for fixed bed hydrotreatment of the effluent obtained from step a), c) a step for hydrocracking of the effluent obtained in step b) in by-passable reactors, d) a step for separation of the effluent obtained from step c).

First claim

The invention claimed is:

1. A continuous process for the treatment of a hydrocarbon feed containing at least one hydrocarbon fraction with a sulphur content of at least 0.1% by weight, an initial boiling temperature of at least 340° C. and a final boiling temperature of at least 440° C., the process comprising:
a) hydrodemetallization in which at least two permutable reactors are operated at a temperature in the range 300° C. to 500° C., and under an absolute pressure in the range 5 MPa to 35 MPa, in the presence of the hydrocarbon feed and hydrogen, and a hydrodemetallization catalyst,
b) fixed bed hydrotreatment, in at least one reactor in which the effluent obtained from a) when is brought into contact with at least one hydrotreatment catalyst at a temperature in the range 300° C. to 500° C. and under an absolute pressure in the range 5 MPa to 35 MPa,
c) fixed bed hydrocracking, in at least one by-passable reactor under an absolute pressure in the range 5 MPa to 35 MPa, in the presence of effluent obtained from b), and a hydrocracking catalyst, in which said by-passable reactor for the fixed bed hydrocracking is stopped as soon as the temperature of said by-passable reactor is between 390° C. and 430° C.,
d) separating effluent obtained from hydrocracking in c) in order to obtain at least one gaseous fraction and at least one heavy liquid fraction, said heavy liquid fraction being sent to an atmospheric distillation producing at least one atmospheric distillate and an atmospheric residue, a portion or the entirety of said atmospheric residue being sent to a vacuum distillation producing a vacuum residue, said atmospheric and vacuum residues optionally being sent to a catalytic cracking process or being used as a fuel oil or fuel oil base.

2. The process for the treatment of a hydrocarbon feed as claimed in claim 1 , in which said by-passable reactor for the fixed bed hydrocracking is stopped as soon as the temperature of said by-passable reactor is between 405° C. and 425° C.

3. The process for the treatment of a hydrocarbon feed as claimed in claim 1 , in which the hydrodemetallization a) is carried out under the following operating conditions:
a temperature in the range 350° C. to 430° C.,
an absolute pressure in the range 11 MPa to 26 MPa,
a HSV (defined as the volumetric flow rate of the feed divided by the total volume of catalyst) in the range 0.1 h −1 to 5 h −1 .

4. The process for the treatment of a hydrocarbon feed as claimed in claim 1 , in which the hydrodemetallization a) employs a hydrodemetallization catalyst comprising 0.5% to 10% by weight of nickel, (expressed as nickel oxide, NiO), and 1% to 30% by weight of molybdenum, (expressed as molybdenum oxide, MoO 3 ) on a mineral support.

5. The process for the treatment of a hydrocarbon feed as claimed in claim 1 , in which the hydrotreatment b) is carried out at a temperature in the range 350° C. to 430° C., and under an absolute pressure in the range 11 MPa to 26 MPa.

6. The process for the treatment of a hydrocarbon feed as claimed in claim 1 , in which the hydrotreatment b) uses a catalyst comprising 0.5% to 10% by weight of nickel, (expressed as nickel oxide NiO), and 1% to 30% by weight of molybdenum (expressed as molybdenum oxide, MoO 3 ) on a mineral support of alumina, silica, silica-alumina, magnesia, clay or mixtures of at least two thereof.

7. The process for the treatment of a hydrocarbon feed as claimed in claim 1 , in which the hydrocracking c) is carried out at a temperature in the range 350° C. to 430° C., and under an absolute pressure in the range 11 MPa to 26 MPa.

8. The process for the treatment of a hydrocarbon feed as claimed in claim 1 , in which the hydrocracking c) employs a catalyst comprising 0.5% to 10% by weight of nickel (expressed as nickel oxide, NiO), and 1% to 30% by weight of molybdenum (expressed as molybdenum oxide, MoO 3 ) on a mineral support of alumina, silica, silica-alumina, magnesia, clay or mixtures of at least two thereof.

9. The process for the treatment of a hydrocarbon feed as claimed in claim 1 , in which the separation d) comprises at least one atmospheric distillation obtaining at least one atmospheric distillate and at least one atmospheric residue, said atmospheric residue being sent to a catalytic cracking process.

10. The process for the treatment of a hydrocarbon feed as claimed in claim 1 , in which the separation d) comprises at least one vacuum distillation obtaining at least one vacuum distillate and at least one vacuum residue.

11. The process for the treatment of a hydrocarbon feed as claimed in claim 1 , in which the hydrodemetallization a) is carried out under the following operating conditions:
a temperature in the range 350° C. to 430° C.,
an absolute pressure in the range 14 MPa to 20 MPa,
a HSV (defined as the volumetric flow rate of the feed divided by the total volume of catalyst) in the range 0.15 h −1 to 3 h −1 .

12. The process for the treatment of a hydrocarbon feed as claimed in claim 1 , in which the hydrodemetallization a) employs a hydrodemetallization catalyst comprising 1% to 5% by weight of nickel, (expressed as nickel oxide, NiO), and 3% to 20% by weight of molybdenum, (expressed as molybdenum oxide, MoO 3 ) on a mineral support.

13. The process for the treatment of a hydrocarbon feed as claimed in claim 1 , in which the hydrotreatment b) uses a catalyst comprising 1% to 5% by weight of nickel, (expressed as nickel oxide NiO), and 5% to 20% by weight of molybdenum (expressed as molybdenum oxide, MoO 3 ) on a mineral support of alumina, silica, silica-alumina, magnesia, clay or mixtures of at least two thereof.

14. The process for the treatment of a hydrocarbon feed as claimed in claim 1 , in which the hydrocracking c) is carried out at a temperature in the range 350° C. to 430° C., and under an absolute pressure in the range of 14 MPa to 20 MPa.

15. The process for the treatment of a hydrocarbon feed as claimed in claim 1 , in which the hydrocracking c) employs a catalyst comprising 1% to 5% by weight of nickel (expressed as nickel oxide, NiO) and 5% to 20% by weight of molybdenum (expressed as molybdenum oxide, MoO 3 ) on a mineral support of alumina, silica, silica-alumina, magnesia, clay or mixtures of at least two thereof.

Assignees

• Ifp Energies Now

Inventors

• Weiss Wilfried
• Tellier Elodie
• Chatron-Michaud Pascal

Classifications

• C10G67/02 Primary

  plural serial stages only · CPC title

• C10G7/06

  Vacuum distillation · CPC title

• C10G65/04

  including only refining steps · CPC title

• C10G2300/1077

  Vacuum residues · CPC title

• C10G2300/205

  Metal content · CPC title