Middle distillate hydrocracking catalyst

Patent metadata

Field	Value
Publication number	US-9944863-B2
Application number	US-201615291823-A
Country	US
Kind code	B2
Filing date	Oct 12, 2016
Priority date	Apr 24, 2014
Publication date	Apr 17, 2018
Grant date	Apr 17, 2018

Abstract

The present invention is directed to an improved hydrocracking catalyst containing an amorphous silica-alumina (ASA) base and alumina support. The ASA base is characterized as having a high nanopore volume and low particle density. The alumina support is characterized as having a high nanopore volume. Hydrocracking catalysts employing the combination high nanopore volume ASA base and alumina support exhibit improved hydrogen efficiency, and greater product yield and quality, as compared to hydrocracking catalysts containing conventional ASA base and alumina components.

First claim

What is claimed is:

1. A hydrocracking catalyst, comprising:
a base extrudate comprising at least one molecular sieve, an alumina and an amorphous silica alumina support, wherein the base extrudate has one or more of the following:
a nanopore volume in the 6 nm to 11 nm range of 0.5 to 0.9 cc/g,
a total nanopore volume in the 2 to 50 nm of 0.7 to 1.2 cc/g,
a particle density of 0.7 to 0.9 g/cc; or
the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g; and

at least one metal selected from the group consisting of elements from Group 6 and Groups 8 through 10 of the Periodic Table.

2. The hydrocracking catalyst of claim 1 , wherein the base extrudate is formed using an alumina having a nanopore volume in the 6 nm to 11 nm range of 0.1 to 0.3 cc/g.

3. The hydrocracking catalyst of claim 2 , wherein the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g.

4. The hydrocracking catalyst of claim 1 , wherein the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g.

5. The hydrocracking catalyst of claim 1 , wherein the base extrudate has a total nanopore volume in the 2 to 50 nm of 0.7 to 1.2 cc/g.

6. The hydrocracking catalyst of claim 1 , wherein the base extrudate has a particle density of 0.7 to 0.9 g/cc.

7. The hydrocracking catalyst of claim 1 , wherein the base extrudate has a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g.

8. A method for making a hydrocracking catalyst, comprising the steps of:
forming a base extrudate comprising at least one molecular sieve, an alumina and an amorphous silica alumina support, wherein the base extrudate has one or more of the following:
a nanopore volume in the 6 nm to 11 nm range of 0.5 to 0.9 cc/g,
a total nanopore volume in the 2 to 50 nm of 0.7 to 1.2 cc/g,
a particle density of 0.7 to 0.9 g/cc; or
the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g; and

impregnating the base extrudate with at least one metal selected from the group consisting of elements from Group 6 and Groups 8 through 10 of the Periodic Table.

9. The method of claim 8 , wherein the base extrudate is formed using an alumina having a nanopore volume in the 6 nm to 11 nm range of 0.1 to 0.3 cc/g.

10. The method of claim 9 , wherein the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g.

11. The method of claim 8 , wherein the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g.

12. The method of claim 8 , wherein the base extrudate has a total nanopore volume in the 2 to 50 nm of 0.7 to 1.2 cc/g.

13. The method of claim 8 , wherein the base extrudate has a particle density of 0.7 to 0.9 g/cc.

14. A process for hydrocracking a hydrocarbonaceous feedstock, comprising contacting the feedstock with a hydrocracking catalyst under hydrocracking conditions to produce a hydrocracked effluent;
the hydrocracking catalyst comprising
a base extrudate comprising at least one molecular sieve, an alumina and an amorphous silica alumina support, wherein the base extrudate has one or more of the following:
a nanopore volume in the 6 nm to 11 nm range of 0.5 to 0.9 cc/g,
a total nanopore volume in the 2 to 50 nm of 0.7 to 1.2 cc/g,
a particle density of 0.7 to 0.9 g/cc; or

the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g; and
at least one metal selected from the group consisting of elements from Group 6 and Groups 8 through 10 of the Periodic Table.

15. The process of claim 14 , wherein the base extrudate is formed using an alumina having a nanopore volume in the 6 nm to 11 nm range of 0.1 to 0.3 cc/g.

16. The process of claim 15 , wherein the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g.

17. The process of claim 14 , wherein the base extrudate is formed using an amorphous silica alumina support having a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g.

18. The process of claim 14 , wherein the base extrudate has a nanopore volume in the 6 nm to 11 nm range of 0.5 to 0.9 cc/g.

19. The process of claim 14 , wherein the base extrudate has a particle density of 0.7 to 0.9 g/cc.

20. The process of claim 14 , wherein the base extrudate has a nanopore volume in the 6 nm to 11 nm range of 0.6 to 0.9 cc/g.

Assignees

• Chevron Usa Inc

Inventors

• Zhang Yihua
• Maesen Theodorus Ludovicus Michael

Classifications

• C10G2300/70

  Catalyst aspects · CPC title

• C10G2300/1044

  Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C · CPC title

• B01J23/888

  Tungsten · CPC title

• B01J29/084

  Y-type faujasite · CPC title

• B01J35/1042

  Operations & Transport · mapped topic