IP Library Granted Patent US 9,340,734
Granted Patent B2
US 9,340,734 · App. 13/513,385 · Granted May 17, 2016

Faujasite zeolite preparation process

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Quick Facts
Patent No.
US 9,340,734
App. No.
13/513,385
Granted
May 17, 2016
Kind
B2
Abstract

Disclosed is a process for the preparation of a faujasite zeolite. A starting zeolite of the faujasite structure having a silica to alumina ratio of from 4.5 to 6.5 and an alkali level of less than 1.5% wt is steam calcined to produce an intermediate zeolite. The intermediate zeolite is treated with an acidified solution having specificately defined characteristics.

Claims (39)

1. A process for the preparation of a zeolite having a unit cell size in the range of from 24.42 to 24.52 Å; a bulk silica to alumina molar ratio (SAR) in the range of from 10 to 15; and a surface area of from 910 to 1020 m 2 /g, which process comprises:

a) providing a starting zeolite of the faujasite structure having a silica to alumina ratio of from 4.5 to 6.5 and an alkali level of less than 1.5% wt;

b) steam calcination by treating said starting zeolite at a temperature in the range of from 550 to 750° C. and at a partial pressure of steam in the range of from 5 to 50 vol %, basis total gas present, for a time effective to produce an intermediate zeolite having a unit cell size of from 24.40 to 24.50 Å;

c) contacting the intermediate zeolite with an acidified solution comprising of from 4 to 9 mmole of acid having a pKa below 0 per gram of zeolite and optionally an ammonium salt under conditions effective to produce a zeolite having a unit cell size in the range of from 24.42 Å to 24.52 Å; a SAR in the range of from 10 to 15; and a surface area of from 910 to 1020 m 2 /g; and

d) recovering said zeolite.

2. A process as claimed in claim 1 , wherein the intermediate zeolite obtained in step b) is treated with an ammonium salt containing aqueous solution before being contacted with the acidified solution of c).

3. A Process for preparing a hydrocracking catalyst carrier composition, which process comprises:

(i) preparing a faujasite zeolite by a process as claimed in claim 2 , and

(ii) mixing the zeolite with amorphous binder component.

4. A process for preparing a hydrocracking catalyst composition which process comprises preparing a catalyst carrier composition according to claim 3 , and further

(iii) incorporating at least one hydrogenation component.

5. A process for converting a hydrocarbonaceous feedstock into lower boiling materials, which comprises contacting the feedstock at elevated temperature and pressure with a hydrocracking catalyst composition obtained in a process as claimed in claim 4 .

6. A process as claimed in claim 1 , wherein the zeolite obtained in step c) is treated with an ammonium salt containing aqueous solution, and optionally washed and dried.

7. A Process for preparing a hydrocracking catalyst carrier composition, which process comprises:

(i) preparing a faujasite zeolite by a process as claimed in claim 6 , and

(ii) mixing the zeolite with amorphous binder component.

8. A process for preparing a hydrocracking catalyst composition which process comprises preparing a catalyst carrier composition according to claim 7 , and further

(iii) incorporating at least one hydrogenation component.

9. A process for converting a hydrocarbonaceous feedstock into lower boiling materials, which comprises contacting the feedstock at elevated temperature and pressure with a hydrocracking catalyst composition obtained in a process as claimed in claim 8 .

10. A process as claimed in any one of claim 1 , wherein the amount of acid having a pKa below 0 is of from 5 to 8 mmole per gram of zeolite.

11. A Process for preparing a hydrocracking catalyst carrier composition, which process comprises:

(i) preparing a faujasite zeolite by a process as claimed in claim 10 , and

(ii) mixing the zeolite with amorphous binder component.

12. A process for preparing a hydrocracking catalyst composition which process comprises preparing a catalyst carrier composition according to claim 11 , and further

(iii) incorporating at least one hydrogenation component.

13. A process for converting a hydrocarbonaceous feedstock into lower boiling materials, which comprises contacting the feedstock at elevated temperature and pressure with a hydrocracking catalyst composition obtained in a process as claimed in claim 12 .

14. A process as claimed in any one of claim 1 , wherein the pH of the acidified solution is at most 4.

15. A Process for preparing a hydrocracking catalyst carrier composition, which process comprises:

(i) preparing a faujasite zeolite by a process as claimed in claim 14 , and

(ii) mixing the zeolite with amorphous binder component.

16. A process for preparing a hydrocracking catalyst composition which process comprises preparing a catalyst carrier composition according to claim 15 , and further

(iii) incorporating at least one hydrogenation component.

17. A process for converting a hydrocarbonaceous feedstock into lower boiling materials, which comprises contacting the feedstock at elevated temperature and pressure with a hydrocracking catalyst composition obtained in a process as claimed in claim 16 .

18. A process for preparing a hydrocracking catalyst carrier composition, which process comprises:

(i) preparing a faujasite zeolite by a process as claimed in claim 1 , and

(ii) mixing the zeolite with amorphous binder component.

19. A process for preparing a hydrocracking catalyst composition which process comprises preparing a catalyst carrier composition according to claim 18 , and further

(iii) incorporating at least one hydrogenation component.

20. A process for converting a hydrocarbonaceous feedstock into lower boiling materials, which comprises contacting the feedstock at elevated temperature and pressure with a hydrocracking catalyst composition obtained in a process as claimed in claim 19 .

Assignments (2)
CHANGE OF NAME Recorded Mar 7, 2022
From: SHELL OIL COMPANY
To: SHELL USA, INC.
Reel/Frame 059694/0819 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 24, 2012
From: DOMOKOS, LASZLO; KIJLSTRA, WIEBE SJOERD; ONG, LAY HWA; CREYGHTON, EDWARD JULIUS
To: SHELL OIL COMPANY
Reel/Frame 028622/0620 →