Systems and processes for conversion of crude oil

Patent metadata

Field	Value
Publication number	US-10689587-B2
Application number	US-201815944068-A
Country	US
Kind code	B2
Filing date	Apr 3, 2018
Priority date	Apr 26, 2017
Publication date	Jun 23, 2020
Grant date	Jun 23, 2020

Abstract

According to an embodiment of the present disclosure, petrochemicals may be produced from crude oil by a process which includes passing the crude oil and hydrogen into a hydroprocessing reactor, separating the hydrotreated oil into a lesser boiling point fraction and a greater boiling point fraction, passing the lesser boiling point fraction to a pyrolysis section of a steam cracker to produce a pyrolysis effluent comprising olefins, aromatics, or both, passing the greater boiling point fraction to a gasifier, where the gasifier produces hydrogen, and passing at least a portion of the hydrogen produced by the gasifier to the hydroprocessing reactor.

First claim

What is claimed is:

1. A process for producing petrochemicals from crude oil, the process comprising:
passing the crude oil and hydrogen into a hydroprocessing reactor, the hydroprocessing reactor comprising one or more hydroprocessing catalysts that produce a hydrotreated oil;
separating the hydrotreated oil into a lesser boiling point fraction and a greater boiling point fraction;
passing the lesser boiling point fraction to a pyrolysis section of a steam cracker to produce a pyrolysis effluent comprising olefins, aromatics, or both;
passing the greater boiling point fraction to a gasifier, where the gasifier produces hydrogen; and
passing at least a portion of the hydrogen produced by the gasifier to the hydroprocessing reactor.

2. The process of claim 1 , where the crude oil is combined with the hydrogen to form a mixed stream which is passed into the hydroproces sing reactor.

3. The process of claim 1 , where the hydroprocessing reactor operates at a temperature of from 300° C. to 450° C. and a hydrogen partial pressure of from 30 to 200 bar.

4. The process of claim 1 , further comprising passing the hydrotreated oil to a convection section of the steam cracker operating at a temperature of from 700° C. to 900° C. to produce a heated hydrotreated oil.

5. The process of claim 1 , further comprising transporting the pyrolysis effluent to at least one separator, where the at least one separator converts the pyrolysis effluent into one or more product streams comprising the olefins, aromatics, or both.

6. The process of claim 1 , where the gasifier operates at a temperature of at least 900° C.

7. The process of claim 1 , where the hydroprocessing reactor comprises one or more of a hydrodemetallization catalyst, hydrocracking catalyst, hydrodearomatization catalyst, hydrodenitrogenation catalyst, or hydrodesulfurization catalyst.

8. The process of claim 7 , where the hydroprocessing reactor comprises a hydrodemetallization catalyst that is disposed upstream of the other hydroprocessing catalysts.

9. The process of claim 1 , where the one or more hydroprocessing catalysts reduce the content of sulfur and metals in the crude oil.

10. The process of claim 1 , where the pyrolysis effluent further comprises hydrogen, which is passed to the hydroproces sing reactor.

11. The process of claim 1 , where the pyrolysis effluent comprises aromatics selected from one or more of benzene, toluene, or xylene.

12. The process of claim 1 , where the gasifier comprises a moving bed system, a fluidized bed system, an entrained-flow system, or combinations thereof.

13. The process of claim 1 , where the greater boiling point fraction comprises a solid material.

14. The process of claim 13 , where the solid material comprises an ash-producing component selected from the group consisting of natural and synthetic oxides of Si, Al, Fe, Ca, Mg, P, K, Na, S, Ti, or combinations thereof.

15. The process of claim 5 , further comprising:
passing hydrogen produced in the separator to a hydrogen purification unit, where the hydrogen purification yields a treated hydrogen stream; and
passing the treated hydrogen stream for mixing with the crude oil upstream of the hydroprocessing reactor.

16. The process of claim 5 , further comprising passing a pyrolysis fuel oil produced in the separator to the gasifier, where the gasifier converts at least a portion of the pyrolysis fuel oil into hydrogen.

17. The process of claim 1 , where the crude oil has an API Gravity of 10 degrees to 40 degrees.

18. The process of claim 1 , further comprising preheating the crude oil to a temperature of at least 300° C. prior to it entering the hydroprocessing reactor.

19. The process of claim 1 , where the greater boiling point fraction comprises vacuum residue.

20. The process of claim 1 , where the gasifier produces hydrogen, carbon monoxide, heated streams, or combinations thereof.

Assignees

• Saudi Arabian Oil Co

Inventors

• Al-Sayed Essam
• Koseoglu Omer Refa
• Ding Lianhui
• Bourane Abdennour
• Ballesteros Alberto Lozano
• Al Jumah Furqan

Classifications

• C10G2400/30

  Aromatics · CPC title

• C10G2300/308

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

• C10G2300/202

  Heteroatoms content, i.e. S, N, O, P · CPC title

• C10G2300/1077

  Vacuum residues · CPC title

• C10G2300/1048

  Middle distillates · CPC title