Manufacturing hydrocracking catalyst

Patent metadata

Field	Value
Publication number	US-11305264-B2
Application number	US-201916569550-A
Country	US
Kind code	B2
Filing date	Sep 12, 2019
Priority date	Sep 12, 2019
Publication date	Apr 19, 2022
Grant date	Apr 19, 2022

Abstract

A method including subjecting an ultra-stable Y-type zeolite having a low silica-to-alumina molar ratio (SAR), such as in a range of 3 to 6, to acid treatment and heteroatom incorporation contemporaneously to give a framework-modified ultra-stable Y-type zeolite.

First claim

What is claimed is:

1. A method of producing a hydrocracking catalyst for hydrocarbon oil, comprising:
exchanging at least 80% of sodium (Na) ions in a Y-type zeolite with ammonium (NH 4 ) ions to convert the Y-type zeolite to an ultra-stable Y-type zeolite comprising a silica-to-alumina molar ratio (SAR) in a range of 3 to 6; and
subjecting the ultra-stable Y-type zeolite comprising the SAR in the range of 3 to 6 to incorporation of heteroatoms and acid treatment simultaneously to give a framework-modified ultra-stable Y-type zeolite comprising an SAR of at least 20, wherein the heteroatoms are incorporated into a framework of the ultra-stable Y-type zeolite, the heteroatoms comprising titanium atoms and further comprising zirconium atoms or hafnium atoms, or both.

2. The method of claim 1 , wherein exchanging at least 80% of Na ions in the Y-type zeolite with NH 4 ions comprises ion exchange and calcination, and wherein the framework-modified ultra-stable Y-type zeolite is a framework-substituted ultra-stable Y-type zeolite in which aluminum atoms in the framework of the ultra-stable Y-type zeolite are replaced with the heteroatoms.

3. The method of claim 1 , wherein the acid treatment and the incorporation of heteroatoms comprise preparing a suspension of the ultra-stable Y-type zeolite in water, adding acid and the heteroatoms to the suspension, and wherein the framework-modified ultra-stable Y-type zeolite comprises an SAR of at least 30.

4. The method of claim 3 , wherein the acid comprises sulfuric acid, nitric acid, hydrochloric acid, or carboxylic acids, or any combinations thereof.

5. The method of claim 3 , wherein adding the heteroatoms to the suspension comprises adding a first aqueous solution comprising the titanium atoms to the suspension and adding a second aqueous solution comprising zirconium atoms or hafnium atoms, or both, to the suspension.

6. The method of claim 3 , wherein the acid treatment and the incorporation of the heteroatoms further comprises neutralizing the suspension to give the framework-modified ultra-stable Y-type zeolite, and wherein the framework-modified ultra-stable Y-type zeolite comprises an SAR in a range of 20 to 100.

7. The method of claim 1 , wherein the framework-modified ultra-stable Y-type zeolite comprises an SAR of at least 40 and a crystal lattice constant in a range of 2.430 nanometers (nm) to 2.450 nm.

8. The method of claim 1 , comprising preparing a support material to be a catalyst support of the hydrocracking catalyst, the support material comprising the framework-modified ultra-stable Y-type zeolite and an inorganic oxide as a granulating agent or binder.

9. The method of claim 8 , wherein the inorganic oxide comprises alumina, silica, titania, silica-alumina, alumina-titania, alumina-zirconia, alumina-boria, phosphorus-alumina, silica-alumina-boria, phosphorus-alumina-boria, phosphorus-alumina-silica, silica-alumina-titania, or silica-alumina-zirconia, or any combinations thereof.

10. The method of claim 8 , comprising impregnating the support material with a hydrogenative metal such that the support material carries the hydrogenative metal.

11. The method of claim 1 , comprising forming the hydrocracking catalyst with the framework-modified ultra-stable Y-type zeolite in a catalyst support of the hydrocracking catalyst, wherein the framework-modified ultra-stable Y-type zeolite comprises a specific surface area in a range of 600 square meter per gram (m 2 /g) to 900 m 2 /g.

12. A method of producing a hydrocracking catalyst, comprising
preparing a suspension of an ultra-stable Y-type zeolite in a liquid, the ultra-stable Y-type zeolite having a silica-to-alumina molar ratio (SAR) in a range of 3 to 6;
performing acid treatment on the ultra-stable Y-type zeolite to increase the SAR of the ultra-stable Y-type zeolite, the acid treatment comprising adding an acid to the suspension;
adding heteroatoms to the suspension simultaneously with performing the acid treatment to incorporate the heteroatoms into a framework of the ultra-stable Y-type zeolite to give a framework-substituted ultra-stable Y-type zeolite having an SAR of at least 20; and
impregnating a hydrogenative metal on a catalyst support comprising the framework-substituted ultra-stable Y-type zeolite.

13. The method of claim 12 , wherein the heteroatoms added to the suspension and incorporated into the framework comprise titanium atoms and further comprise zirconium atoms or hafnium atoms, or both, wherein to incorporate the heteroatoms into the framework comprises to replace aluminum atoms in the framework with the heteroatoms, and wherein the framework-substituted ultra-stable Y-type zeolite has an SAR of at least 30.

14. The method of claim 12 , comprising replacing at least 80% of sodium (Na) ions in a Y-type zeolite with ammonium (NH 4 ) ions to give the ultra-stable Y-type zeolite, and wherein the framework-substituted ultra-stable Y-type zeolite comprises a specific surface area in the range of 600 square meter per gram (m 2 /g) to 900 m 2 /g.

15. The method of claim 14 , wherein replacing at least 80% of Na ions in the Y-type zeolite with NH 4 ions comprises ion exchange and calcination, wherein the suspension comprises a mass ratio of the liquid to solid in a range of 5 to 15, wherein the liquid in the suspension comprises water, and wherein the framework-substituted ultra-stable Y-type zeolite has an SAR of at least 40.

16. The method of claim 12 , wherein the framework-substituted ultra-stable Y-type zeolite comprises a crystal lattice constant in a range of 2.430 nanometers (nm) to 2.450 nm, and wherein the hydrogenative metal is less than 40% by mass of the hydrocracking catalyst.

17. The method of claim 12 , comprising forming the hydrocracking catalyst with a catalyst support comprising the framework-substituted ultra-stable Y-type zeolite, and wherein the framework-substituted ultra-stable Y-type zeolite comprises an SAR in a range of 30 to 100.

18. The method of claim 12 , wherein the hydrogenative metal comprises a metal component comprising iron, cobalt, nickel, rhodium, palladium, silver, iridium, platinum, gold, chromium, molybdenum, or tungsten, or any combinations thereof.

19. A method of forming a framework-modified ultra-stable Y-type zeolite for a catalyst support of a hydrocracking catalyst, comprising:
subjecting an ultra-stable Y-type zeolite having a silica-to-alumina molar ratio (SAR) in a range of 3 to 6 to incorporation of heteroatoms and acid treatment simultaneously to give the framework-modified ultra-stable Y-type zeolite; and
wherein the framework-modified ultra-stable Y-type zeolite comprises an SAR of at least 30 and a specific surface area of at least 600 square meter per gram (m 2 /g).

20. The method of claim 19 , comprising:
performing a first ion-exchange on a Y-type zeolite to exchange sodium ions of the Y-type zeolite with ammonium ions to give a first ammonium-exchanged Y-type zeolite;
calcining the first ammonium-exchanged Y-type zeolite;
performing a second ion-exchange on the first ammonium-exchanged Y-type zeolite as calcined to exchange sodium ions of the first ammonium-exchanged Y-type zeolite as calcined with ammonium ions to give a second ammonium-exchanged Y-type zeolite; and
calcining the second ammonium-exchanged Y-type zeolite to give the ultra-stable Y-type zeolite.

21. The method of claim 20 , wherein at least 80% of sodium ions in the Y-type zeolite are replaced with ammonium ions, and wherein the framework-modified

Assignees

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

Inventors

• Hodgkins Robert Peter
• Koseoglu Omer Refa
• Uchida Koji
• Kagawa Tomoyasu
• Watabe Mitsunori

Classifications

• C10G2300/70

  Catalyst aspects · CPC title

• C10G49/08

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

• C10G49/06

  containing platinum group metals or compounds thereof · CPC title

• C10G49/04

  containing nickel, cobalt, chromium, molybdenum, or tungsten metals, or compounds thereof · CPC title

• C10G47/20

  the catalyst containing other metals or compounds thereof · CPC title