FCC catalyst compositions for fluid catalytic cracking and methods of using the FCC catalyst compositions

Patent metadata

Field	Value
Publication number	US-11446645-B2
Application number	US-202016919336-A
Country	US
Kind code	B2
Filing date	Jul 2, 2020
Priority date	Jul 2, 2020
Publication date	Sep 20, 2022
Grant date	Sep 20, 2022

Abstract

A fluid catalytic cracking catalyst composition (FCC catalyst composition) includes a framework-substituted ultra-stable Y-type zeolite (USY zeolite) having one or more transition metals substituted into the framework of a USY zeolite and a FCC zeolite cracking additive. A method for upgrading a hydrocarbon feed includes contacting the hydrocarbon feed with the FCC catalyst composition of the present disclosure at reaction conditions sufficient to upgrade at least a portion of the hydrocarbon feed. A method for upgrading a hydrocarbon feed includes passing the hydrocarbon feed to a fluid catalytic cracking unit, contacting the hydrocarbon feed with a FCC catalyst composition in the fluid catalytic cracking unit under reaction conditions sufficient to cause at least a portion of the hydrocarbon feed to undergo cracking reactions to produce a cracking reaction mixture comprising a used FCC catalyst composition and a cracked effluent comprising one or more olefins.

First claim

What is claimed is:

1. A fluid catalytic cracking (FCC) catalyst composition comprising
a framework-substituted USY zeolite comprising one or more transition metals substituted into the framework of an USY zeolite;
from 1 weight percent to 50 weight percent FCC zeolite cracking additive based on the total weight of the FCC catalyst composition, and
from 35 weight percent to 60 weight percent inorganic filler based on the total weight of the FCC catalyst composition, where the inorganic filler comprises one or more of silica sol, basic aluminum chloride, aluminum biphosphate, alumina sol, activated alumina, porous silica, a metal trapping agent, or combinations of these.

2. The FCC catalyst composition of claim 1 , in which the one or more transition metals comprises hafnium, zirconium, titanium, or combinations of these.

3. The FCC catalyst composition of claim 1 , in which the framework-substituted USY zeolite comprises a crystal lattice constant from 2.430 nanometers to 2.450 nanometers and a specific surface area from 600 square meters per gram to 900 square meters per gram.

4. The FCC catalyst composition of claim 1 , in which the FCC catalyst composition comprises from 5 weight percent to 60 weight percent framework-substituted USY zeolite based on the total weight of the FCC catalyst composition.

5. The FCC catalyst composition of claim 1 , in which the FCC catalyst composition comprises from 5 weight percent to 15 weight percent FCC zeolite cracking additive based on the total weight of the FCC catalyst composition.

6. The FCC catalyst composition of claim 1 , in which the FCC zeolite cracking additive comprises a MFI-framework zeolite.

7. The FCC catalyst composition of claim 1 , in which the FCC zeolite cracking additive comprises a ZSM-5 zeolite.

8. A method for upgrading a hydrocarbon feed, the method comprising:
contacting the hydrocarbon feed with a FCC catalyst composition at reaction conditions sufficient to upgrade at least a portion of the hydrocarbon feed, where:
the FCC catalyst composition comprises:
a framework-substituted USY zeolite, where the framework-substituted USY zeolite comprises hafnium, zirconium, titanium, or combinations of these substituted into the framework of the framework-substituted USY zeolite;
from 1 weight percent to 50 weight percent FCC zeolite cracking additive based on the total weigh to the FCC catalyst composition; and
from 35 weight percent to 60 weight percent inorganic filler based on the total weight of the FCC catalyst composition, where the inorganic filler comprises one or more of silica sol, basic aluminum chloride, aluminum biphosphate, alumina sol, activated alumina, porous silica, a metal trapping agent, or combinations of these.

9. The method for upgrading the hydrocarbon feed of claim 8 , in which the hydrocarbon feed is contacted with the FCC catalyst composition at a hydrocarbon feed to FCC catalyst composition mass ratio from 1:2 to 1:30, for a residence time from 0.1 seconds to 60 seconds, and a temperature of from 450 degrees Celsius to 700 degrees Celsius.

10. The method for upgrading the hydrocarbon feed of claim 8 , in which the one or more transition metals further comprises zirconium or titanium.

11. The method for upgrading the hydrocarbon feed of claim 8 , in which the FCC catalyst composition comprises from 5 weight percent to 60 weight percent framework-substituted USY zeolite based on the total weight of the FCC catalyst composition.

12. The method for upgrading the hydrocarbon feed of claim 8 , further comprising from 15 weight percent to 60 weight percent inorganic filler based on the total weight of the FCC catalyst composition.

13. The method for upgrading the hydrocarbon feed of claim 8 , in which the FCC catalyst composition comprises from 5 weight percent to 15 weight percent FCC zeolite cracking additive based on the total weight of the FCC catalyst composition.

14. The method for upgrading the hydrocarbon feed of claim 8 , in which the FCC zeolite cracking additive comprises a MFI-framework zeolite.

15. The method for upgrading the hydrocarbon feed of claim 8 , in which the FCC zeolite cracking additive comprises a ZSM-5 zeolite.

16. A method for upgrading a hydrocarbon feed, the method comprising
passing a hydrocarbon feed to a fluid catalytic cracking unit;
contacting the hydrocarbon feed with a FCC catalyst composition in the fluid catalytic cracking unit under reaction conditions sufficient to cause at least a portion of the hydrocarbon feed to undergo cracking reactions to produce a cracking reaction mixture comprising a used FCC catalyst composition and a cracked effluent comprising one or more olefins, where the FCC catalyst composition comprises:
a framework-substituted USY zeolite comprising, hafnium, zirconium, titanium, or combinations of these substituted into the framework of the framework-substituted USY zeolite; and
from 1 weight percent to 50 weight percent FCC zeolite cracking additive based on the total weight of the FCC catalyst, where the FCC zeolite cracking additive is an MEL-framework zeolite, a beta framework zeolite, a mordenite framework zeolite, or combinations of these;
passing the cracking reaction mixture to a catalyst separator that separates the cracking reaction mixture into the used FCC catalyst composition and the cracked effluent; and
passing the cracked effluent out of the fluid catalytic cracking unit.

17. The method for upgrading the hydrocarbon feed of claim 16 , in which the hydrocarbon feed is contacted with the FCC catalyst composition at a hydrocarbon feed to FCC catalyst composition mass ratio from 1:2 to 1:30.

18. The method for upgrading the hydrocarbon feed of claim 16 , in which the one or more transition metals further comprises zirconium or titanium.

19. The method for upgrading the hydrocarbon feed of claim 16 , in which the FCC catalyst composition comprises from 5 weight percent to 60 weight percent framework-substituted USY zeolite based on the weight of the FCC catalyst composition.

20. The method for upgrading the hydrocarbon feed of claim 16 , in which the FCC zeolite cracking additive comprises a MFI-framework zeolite.

Assignees

• Saudi Arabian Oil Co
• Jgc Catalysts & Chemicals Ltd
• Japan Coop Center Petroleum

Inventors

• Koseoglu Omer Refa
• Jin Yaming
• Ushio Masaru
• Arakawa Seiji

Classifications

• B01J2029/062

  Mixtures of different aluminosilicates · CPC title

• C10G2300/70

  Catalyst aspects · CPC title

• C10G11/05

  Crystalline alumino-silicates, e.g. molecular sieves · CPC title

• C10G11/18

  according to the "fluidised-bed" technique · CPC title

• B01J29/088 Primary

  Y-type faujasite · CPC title