Integrated hydrotreating and hydrocracking with continuous hydrotreating catalyst regeneration

Patent metadata

Field	Value
Publication number	US-11859140-B2
Application number	US-202217590937-A
Country	US
Kind code	B2
Filing date	Feb 2, 2022
Priority date	Feb 2, 2022
Publication date	Jan 2, 2024
Grant date	Jan 2, 2024

Abstract

An integrated hydrotreating and hydrocracking process includes contacting a hydrocarbon oil stream with a hydrogen stream and a hydrotreating catalyst in a moving-bed hydrotreating reactor, thereby producing a hydrocarbon product stream and a spent hydrotreating catalyst; contacting the hydrocarbon product stream with a second hydrogen stream and a hydrocracking catalyst in a hydrocracking reactor, thereby producing a hydrocracked hydrocarbon product stream; processing the spent hydrotreating catalyst to produce regenerated hydrotreating catalyst; and recycling the regenerated hydrotreating catalyst to the moving-bed hydrotreating reactor.

First claim

What is claimed is:

1. An integrated hydrotreating and hydrocracking process comprising:
contacting a hydrocarbon oil stream with a hydrogen stream and a hydrotreating catalyst in a moving-bed hydrotreating reactor to hydrotreat the hydrocarbon oil stream, thereby producing a hydrotreated hydrocarbon product stream and a spent hydrotreating catalyst;
contacting the hydrotreated hydrocarbon product stream with a second hydrogen stream and a hydrocracking catalyst in a hydrocracking reactor to crack the hydrotreated hydrocarbon oil stream, thereby producing a hydrocracked hydrocarbon product stream;
processing the spent hydrotreating catalyst to produce regenerated hydrotreating catalyst; and
recycling the regenerated hydrotreating catalyst to the moving-bed hydrotreating reactor.

2. The integrated hydrotreating and hydrocracking process of claim 1 , wherein the moving-bed hydrotreating reactor is an ebullated-bed hydrotreating reactor.

3. The integrated hydrotreating and hydrocracking process of claim 2 , wherein the hydrotreating catalyst has an average particle size from 500 μm to 1000 μm.

4. The integrated hydrotreating and hydrocracking process of claim 1 , further comprising:
separating the hydrotreated hydrocarbon product stream from the spent hydrotreating catalyst, and wherein
the moving-bed hydrotreating reactor is a slurry-bed hydrotreating reactor.

5. The integrated hydrotreating and hydrocracking process of claim 4 , wherein the hydrotreating catalyst has an average particle size from 0.01 μm to 10 μm.

6. The integrated hydrotreating and hydrocracking process of claim 1 , wherein processing the spent hydrotreating catalyst comprises:
stripping the spent hydrotreating catalyst; and
regenerating the spent hydrotreating catalyst by thermal treatment, and wherein
stripping and regenerating the spent hydrotreating catalyst at least partially removes coke deposited on the spent hydrotreating catalyst, thereby producing the regenerated hydrotreating catalyst.

7. The integrated hydrotreating and hydrocracking process of claim 6 , further comprising;
mixing the regenerated hydrotreating catalyst with fresh hydrotreating catalyst to produce a catalyst mixture;
presulfiding the catalyst mixture to produce a presulfided hydrotreating catalyst; and
recycling the presulfided hydrotreating catalyst to the moving-bed hydrotreating reactor.

8. The integrated hydrotreating and hydrocracking process of claim 1 , wherein the hydrocarbon oil stream comprises whole crude oil, topped crude oil, or both.

9. The integrated hydrotreating and hydrocracking process of claim 1 , wherein the hydrotreating catalyst comprises MoNi on Al 2 O 3 , MoCO on Al 2 O 3 , MoS 2 , maghemite, Fe 3 O 4 , nickel, NiO, TiO 2 , ZrO 2 , CeO 2 , or combinations thereof.

10. The integrated hydrotreating and hydrocracking process of claim 1 , wherein the hydrocracking catalyst comprises an active metal and a support, the active metal comprising NiMo, NiW, or a combination thereof, and the support comprising nano-sized zeolite, hierarchical zeolite, or a combination thereof.

11. The integrated hydrotreating and hydrocracking process of claim 1 , wherein the moving-bed hydrotreating reactor has a temperature from 370° C. to 500° C., a pressure from 12 MPa to 16 MPa, or both.

12. The integrated hydrotreating and hydrocracking process of claim 1 , wherein the moving-bed hydrotreating reactor has a liquid hourly space velocity from 0.2 h −1 to 0.7 h −1 and a ratio of hydrogen stream to hydrocarbon oil stream from 800 L/L to 1200 L/L.

13. The integrated hydrotreating and hydrocracking process of claim 1 , wherein the hydrocracking reactor has a temperature from 350° C. to 440° C., a pressure from 13 MPa to 16 MPa, or both.

14. The integrated hydrotreating and hydrocracking process of claim 1 , wherein the hydrocracking reactor has a liquid hourly space velocity from 0.5 h −1 to 1.5 h −1 and a ratio of hydrogen stream to the hydrocarbon product stream from 1000 L/L to 2000 L/L.

15. A system for hydrotreating and hydrocracking a hydrocarbon oil stream, the system comprising:
a moving-bed hydrotreating reactor configured to hydrotreat the hydrocarbon oil stream and a hydrogen stream with a hydrotreating catalyst to hydrotreat the hydrocarbon oil stream and form a hydrotreated hydrocarbon product stream and spent hydrotreating catalyst;
a hydrocracking reactor fluidly connected to the moving-bed hydrotreating reactor and configured to crack the hydrotreated hydrocarbon product stream and a second hydrogen stream to form a hydrocracked hydrocarbon product stream;
a stripper fluidly connected to the moving-bed hydrotreating reactor and configured to strip the spent hydrotreating catalyst to form a stripped hydrotreating catalyst; and
a catalyst regenerator fluidly connected to the stripper and the moving-bed hydrotreating reactor and configured to regenerate the stripped hydrotreating catalyst to form a regenerated hydrotreating catalyst.

16. The system of claim 15 , wherein:
the moving-bed hydrotreating reactor is an ebullated-bed hydrotreating reactor; and
the catalyst regenerator is configured to send the regenerated hydrotreating catalyst to the moving-bed hydrotreating reactor.

17. The system of claim 15 , wherein the system further comprises:
a catalyst separator fluidly connected to the moving-bed hydrotreating reactor, the hydrocracking reactor, and the stripper, wherein
the moving-bed hydrotreating reactor is a slurry-bed hydrotreating reactor; and
the catalyst separator is configured to separate the hydrotreated hydrocarbon product stream from the spent hydrotreating catalyst.

18. The system of claim 15 , wherein the system further comprises:
a presulfiding unit fluidly connected to the catalyst regenerator and the moving-bed hydrotreating reactor, wherein
the presulfiding unit is configured to presulfide the regenerated hydrotreating catalyst to form a presulfided regenerated hydrotreating catalyst; and
the presulfiding unit is configured to send the presulfided regenerated hydrotreating catalyst to the moving-bed hydrotreating reactor.

19. The system of claim 15 , wherein the hydrocarbon oil stream comprises whole crude oil, topped crude oil, or both.

20. The system of claim 15 , wherein the system further comprises:
a separator fluidly connected to the hydrocracking reactor and configured to separate the hydrocracked hydrocarbon product stream into a light fraction stream comprising C 1 -C 4 hydrocarbons, hydrogen sulfide, hydrogen, ammonia, or combinations thereof and a heavy hydrocarbon fraction stream comprising C 5+ hydrocarbons;
a scrubbing unit fluidly connected to the separator and configured to separate the C 1 -C 4 hydrocarbons and hydrogen from the hydrogen sulfide and ammonia;
a pressure swing adsorption (PSA) unit fluidly connected to the scrubbing unit and configured to separate the hydrogen from the C 1 -C 4 hydrocarbons;
a methane cracking unit fluidly connected to the scrubbing unit and configured to crack the C 1 -C 4 hydrocarbons and separate methane from C 2 -C 4 hydrocarbons;
a steam cracking unit fluidly connected to the separator and methane cracking unit and configured to steam crack the C 2 -C 4 hydrocarbons and the C 5+ hydrocarbons; and
an aromatization process unit fluidly connected to the steam cracking unit and configured to separate aromatic hydrocarbons from the C 2 -C 5+ hydrocarbons.

Assignees

• Saudi Arabian Oil Co

Inventors

• Ding Lianhui
• Zhang Zhonglin
• Al-Bogami Saad A
• Al-Ghamdi Sameer A

Classifications

• B01J38/12

  Treating with free oxygen-containing gas · CPC title

• B01J29/90

  Regeneration or reactivation · CPC title

• B01J29/166

  Y-type faujasite · CPC title

• B01J23/883

  and nickel · CPC title

• C10G47/16

  Crystalline alumino-silicate carriers · CPC title