Systems and methods for upgrading heavy oils

Patent metadata

Field	Value
Publication number	US-11084992-B2
Application number	US-201715605575-A
Country	US
Kind code	B2
Filing date	May 25, 2017
Priority date	Jun 2, 2016
Publication date	Aug 10, 2021
Grant date	Aug 10, 2021

Abstract

In accordance with one embodiment of the present disclosure, a heavy oil may be upgraded by a process that may include removing at least a portion of metals from the heavy oil in a hydrodemetalization reaction zone to form a hydrodemetalization reaction effluent, removing at least a portion of metals and at least a portion of nitrogen from the hydrodemetalization reaction effluent in a transition reaction zone to form a transition reaction effluent, removing at least a portion of nitrogen from the transition reaction effluent in a hydrodenitrogenation reaction zone to form a hydrodenitrogenation reaction effluent, and reducing aromatics content in the hydrodenitrogenation reaction effluent in a hydrocracking reaction zone by contacting the hydrodenitrogenation reaction effluent to form an upgraded fuel.

First claim

What is claimed is:

1. A process for upgrading heavy oil, the process comprising:
removing at least a portion of metals from the heavy oil in a hydrodemetalization reaction zone to form a hydrodemetalization reaction effluent;
removing at least a portion of metals and at least a portion of nitrogen from the hydrodemetalization reaction effluent in a transition reaction zone to form a transition reaction effluent, where the transition reaction zone is positioned downstream of the hydrodemetalization reaction zone;
removing at least a portion of nitrogen from the transition reaction effluent in a hydrodenitrogenation reaction zone to form a hydrodenitrogenation reaction effluent, where the hydrodenitrogenation reaction zone is positioned downstream of the transition reaction zone;
reducing aromatics content in the hydrodenitrogenation reaction effluent in a hydrocracking reaction zone to form an upgraded fuel, where:
the hydrocracking reaction zone is positioned downstream of the hydroprocessing reaction zone;
the hydrocracking reaction zone comprises a hydrocracking catalyst comprising a mesoporous zeolite and one or more metals, where the mesoporous zeolite has an average pore size of from 2 nm to 50 nm;
the aromatics content is reduced in the hydrodenitrogenation reaction effluent in the hydrocracking reaction zone by contacting the hydrodenitrogenation reaction effluent with the hydrocracking catalyst; and
the hydrodenitrogenation reaction zone comprises a hydrodenitrogenation catalyst comprising one or more metals on an alumina support, the alumina support having an average pore size of from 25 nm to 50 nm.

2. The process of claim 1 , where the hydrodemetalization reaction zone comprises a hydrodemetalization catalyst, and the metal is removed from the heavy oil in the hydrodemetalization reaction zone by contacting the heavy oil with the hydrodemetalization catalyst, where the hydrodemetalization catalyst comprises molybdenum.

3. The process of claim 1 , where the transition reaction zone comprises a transition catalyst, and the metal and nitrogen is removed from the hydrodemetalization reaction effluent in the transition reaction zone by contacting the hydrodemetalization reaction effluent with the transition catalyst, where the transition catalyst comprises molybdenum and nickel.

4. The process of claim 1 , where the hydrodenitrogenation reaction zone comprises a hydrodenitrogenation catalyst, and the nitrogen is removed from the transition reaction effluent in the hydrodenitrogenation reaction zone by contacting the transition reaction effluent with the hydrodenitrogenation catalyst, where the hydrodenitrogenation catalyst comprises molybdenum and nickel.

5. The process of claim 1 , where the hydrodenitrogenation catalyst comprises:
from 10 wt. % to 18 wt. % of an oxide or sulfide of molybdenum;
from 2 wt. % to 8 wt. % of an oxide or sulfide of nickel; and
from 74 wt. % to 88 wt. % of alumina.

6. The process of claim 1 , where hydrocracking catalyst comprises tungsten and nickel.

7. The process of claim 1 , where the hydrocracking catalyst comprises:
from 18 wt. % to 28 wt. % of an oxide or sulfide of tungsten;
from 2 wt. % to 8 wt. % of an oxide or sulfide of nickel; and
from 5 wt. % to 40 wt. % of zeolite.

8. The process of claim 1 , where hydrocracking catalyst comprises molybdenum and nickel.

9. The process of claim 1 , where the hydrocracking catalyst comprises:
from 12 wt. % to 18 wt. % of an oxide or sulfide of molybdenum;
from 2 wt. % to 8 wt. % of an oxide or sulfide of nickel; and
from 5 wt. % to 40 wt. % of zeolite.

10. The process of claim 1 , where the heavy oil comprises crude oil, where the crude oil has an American Petroleum Institute (API) gravity of from 25 degrees to 50 degrees.

11. The process of claim 1 , further comprising processing the upgraded fuel to form one or more petrochemical fractions.

12. The process of claim 1 , where the processing of the upgraded fuel comprises a hydrocracking process.

13. The process of claim 1 , where the processing of the upgraded fuel comprises fluid catalytic cracking.

14. A process for upgrading heavy oil, the process comprising:
introducing a stream comprising the heavy oil to a hydrodemetalization reaction zone comprising hydrodemetalization catalyst;
removing at least a portion of metals from the heavy oil in a hydrodemetalization reaction zone to form a hydrodemetalization reaction effluent;
passing the hydrodemetalization reaction effluent from the hydrodemetalization reaction zone to a transition reaction zone comprising a transition catalyst;
removing at least a portion of metals and a portion of nitrogen from the hydrodemetalization reaction effluent in the transition reaction zone to form a transition reaction effluent;
passing the transition reaction effluent from the transition reaction zone to a hydrodenitrogenation reaction zone comprising a hydrodenitrogenation catalyst, where the hydrodenitrogenation catalyst comprises one or more metals on an alumina support, the alumina support having an average pore size of from 25 nm to 50 nm;
removing at least a portion of nitrogen from the transition reaction effluent in the hydrodenitrogenation reaction zone to form a hydrodenitrogenation reaction effluent;
passing the hydrodenitrogenation reaction effluent to a hydrocracking reaction zone comprising a hydrocracking catalyst, where the hydrocracking catalyst comprises a mesoporous zeolite and one or more metals, where the mesoporous zeolite has an average pore size of from 2 nm to 50 nm; and
reducing aromatics content in the hydrodenitrogenation reaction effluent in the hydrocracking reaction zone to form an upgraded fuel.

15. The process of claim 14 , where hydrocracking catalyst comprises tungsten and nickel.

16. The process of claim 14 , where hydrocracking catalyst comprises molybdenum and nickel.

17. A hydroprocessing reactor comprising:
a hydrodemetalization catalyst;
a transition catalyst positioned downstream of the hydrodemetalization catalyst;
a hydrodenitrogenation catalyst positioned downstream of the transition catalyst, where the hydrodenitrogenation catalyst comprises one or more metals on an alumina support, the alumina support having an average pore size of from 25 nm to 50 nm; and
a hydrocracking catalyst positioned downstream of the hydrodenitrogenation catalyst, the hydrocracking catalyst comprising a mesoporous zeolite and one or more metals, where the mesoporous zeolite has an average pore size of from 2 nm to 50 nm.

18. The process of claim 17 , where hydrocracking catalyst comprises tungsten and nickel.

19. The process of claim 17 , where hydrocracking catalyst comprises molybdenum and nickel.

20. A process for upgrading heavy oil, the process comprising:
removing at least a portion of metals from the heavy oil in a hydrodemetalization reaction zone to form a hydrodemetalization reaction effluent;
removing at least a portion of metals and at least a portion of nitrogen from the hydrodemetalization reaction effluent in a transition reaction zone to form a transition reaction effluent, where the transition reaction zone is positioned downstream of the hydrodemetalization reaction zone;
removing at least a portion of nitrogen from the transition reaction effluent in a hydrodenitrogenation reaction zone to form a hydrodenitrogenation reaction effluent, where:
the hydrodenitrogenation reaction zone is positioned downstream of the transition reaction zone; and
the hydrodenitrogenation re

Assignees

• Saudi Arabian Oil Co

Inventors

• Ding Lianhui
• Al-Sayed Essam
• Abba Ibrahim

Classifications

• C10G2300/308

  Gravity, density, e.g. API · CPC title

• C10G69/04 Primary

  including at least one step of catalytic cracking in the absence of hydrogen · CPC title

• C10G69/02

  plural serial stages only · CPC title

• C10G67/02

  plural serial stages only · CPC title

• C10G65/12

  including cracking steps and other hydrotreatment steps · CPC title