Systems and methods for the conversion of heavy oils to petrochemical products

Patent metadata

Field	Value
Publication number	US-10793792-B2
Application number	US-201715799338-A
Country	US
Kind code	B2
Filing date	Oct 31, 2017
Priority date	May 15, 2017
Publication date	Oct 6, 2020
Grant date	Oct 6, 2020

Abstract

According to one or more embodiments presently described, a feedstock oil may be processed by a method which may include hydrotreating the feedstock oil to reduce or remove one or more of sulfur content, metals content, nitrogen content, or aromatics content to produce a hydrotreated oil stream; separating at least a portion of the hydrotreated oil stream into a at least a lesser boiling point oil fraction stream and a greater boiling point oil fraction stream in a first separator; hydrocracking the greater boiling point oil fraction stream; and steam cracking the lesser boiling point oil fraction stream.

First claim

What is claimed is:

1. A method for processing a feedstock oil, the method comprising:
hydrotreating the feedstock oil to reduce or remove one or more of sulfur content, metals content, nitrogen content, or aromatics content to produce a hydrotreated oil stream;
separating at least a portion of the hydrotreated oil stream into only a lesser boiling point oil fraction stream and a greater boiling point oil fraction stream in a flash drum;
hydrocracking the greater boiling point oil fraction stream; and
steam cracking the lesser boiling point oil fraction stream.

2. The method of claim 1 , wherein the feedstock oil is crude oil.

3. The method of claim 2 , wherein the crude oil has an American Petroleum Institute (API) gravity of from 22 degrees to 40 degrees.

4. The method of claim 1 , wherein a hydrocracked effluent stream is formed by the hydrocracking of the greater boiling point oil fraction stream, and wherein the hydrocracked effluent stream is recycled to the hydrotreated oil stream.

5. The method of claim 1 , wherein the steam cracking of at least the lesser boiling point oil fraction forms a steam-cracked effluent stream comprising one or more of pyrolysis oil, gasoline, mixed butenes, hydrogen, methane, butane, butene, propane, propene, ethylene, ethane, benzene, toluene, or xylene.

6. The method of claim 1 , wherein the steam cracking of at least the lesser boiling point oil fraction forms a steam-cracked effluent stream, and wherein the steam-cracked effluent stream is separated into one or more system product streams and a pyrolysis oil stream.

7. The method of claim 6 , wherein the pyrolysis oil stream is passed to the first separator.

8. The method of claim 1 , wherein the feedstock oil is hydrotreated in a hydrotreating unit comprising two or more catalysts in series.

9. A method for processing a feedstock oil, the method comprising:
hydrotreating the feedstock oil to reduce or remove one or more of sulfur content, metals content, nitrogen content, or aromatics content to produce a hydrotreated oil stream;
separating the hydrotreated oil stream into at least a liquid hydrotreated oil stream and a gas hydrotreated oil stream in a first separator;
separating the liquid hydrotreated oil stream into only a lesser boiling point oil fraction stream and a greater boiling point oil fraction stream in a flash drum;
hydrocracking the greater boiling point oil fraction stream to from a hydrocracked effluent stream;
passing the hydrocracked effluent stream to the first separator; and
steam cracking the lesser boiling point oil fraction stream.

10. The method of claim 9 , wherein the gas hydrotreated oil stream is processed in a gas plant to form a gas plant effluent stream.

11. The method of claim 10 , wherein the gas plant effluent stream is steam cracked.

12. The method of claim 9 , wherein the steam cracking of at least the lesser boiling point oil fraction forms a steam-cracked effluent stream comprising one or more of pyrolysis oil, gasoline, mixed butenes, hydrogen, methane, butane, butene, propane, propene, ethylene, ethane, benzene, toluene, or xylene.

13. The method of claim 9 , wherein the steam cracking of at least the lesser boiling point oil fraction forms a steam-cracked effluent stream, and wherein the steam-cracked effluent stream is separated into one or more system product streams and a pyrolysis oil stream.

14. The method of claim 13 , wherein the pyrolysis oil stream is passed to the second separator.

15. The method of claim 9 , wherein the feedstock oil is crude oil.

16. A method for processing a feedstock oil, the method comprising:
hydrotreating the feedstock oil to reduce or remove one or more of sulfur content, metals content, nitrogen content, or aromatics content to produce a hydrotreated oil stream;
separating the hydrotreated oil stream into at least a liquid hydrotreated oil stream and a gas hydrotreated oil stream in a first separator;
separating the liquid hydrotreated oil stream into only a lesser boiling point oil fraction stream and a greater boiling point oil fraction stream in a flash drum;
hydrocracking the greater boiling point oil fraction stream to from a hydrocracked effluent stream;
separating the hydrocracked effluent stream into at least a gas hydrocracked stream and a liquid hydrocracked stream; and
steam cracking the liquid hydrocracked stream.

17. The method of claim 16 , further comprising combining the gas hydrocracked stream with the gas hydrotreated oil stream.

18. The method of claim 16 , further comprising combining the liquid hydrocracked stream with the lesser boiling point oil fraction stream.

19. The method of claim 16 , wherein the feedstock oil is crude oil.

Assignees

• Saudi Arabian Oil Co

Inventors

• Ding Lianhui
• Al-Sayed Essam
• Mohamed Sherif
• Al-Nutaifi Ibrahim
• Ballesteros Alberto Lozano
• Abba Ibrahim

Classifications

• C10G2400/22

  Higher olefins · CPC title

• C10G2400/02

  Gasoline · CPC title

• C10G2300/205

  Metal content · CPC title

• C10G2300/202

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

• C10G69/14

  plural parallel stages only · CPC title