IP Library Granted Patent US 12,479,736
Granted Patent B2
US 12,479,736 · App. 18/168,889 · Granted Nov 25, 2025

Mesoporous zeolites and methods of making the same

Inventors: Faisal Alotaibi (Al-Khobar, SA); Lianhui Ding (Dhahran, SA)
Assignee: Saudi Arabian Oil Company
C01B39/026C01B39/04C01B39/24C01P2006/12C01P2006/14C01P2006/16
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Quick Facts
Patent No.
US 12,479,736
App. No.
18/168,889
Granted
Nov 25, 2025
Kind
B2
Abstract

A method of making a mesoporous zeolite may include combining an initial zeolite with cetyltrimethylammonium bromide to form an initial zeolite mixture. The method may also include adding ammonium hexafluorosilicate and ammonium hydroxide to the initial zeolite mixture to form a treated zeolite mixture. The method may also include heating the treated zeolite mixture to form the mesoporous zeolite.

Claims (24)

1 . A method of making a mesoporous zeolite, the method comprising:

combining an initial zeolite with cetyltrimethylammonium bromide to form an initial zeolite mixture;

adding ammonium hexafluorosilicate and ammonium hydroxide to the initial zeolite mixture to form a treated zeolite mixture; and

heating the treated zeolite mixture to form the mesoporous zeolite.

2 . The method of claim 1 , wherein the initial zeolite mixture is not exposed to steam prior to forming the treated zeolite mixture.

3 . The method of claim 1 , wherein the method does not comprise one or more of drying, filtering, or calcining the initial zeolite mixture prior to forming the treated zeolite mixture.

4 . The method of claim 1 , wherein the initial zeolite comprises a Y zeolite.

5 . The method of claim 1 , wherein the ammonium hexafluorosilicate and ammonium hydroxide added to the initial zeolite are in an aqueous solution.

6 . The method of claim 5 , wherein the concentration of the ammonium hexafluorosilicate in the aqueous solution is from 0.1 M to 2.0 M.

7 . The method of claim 5 , wherein the concentration of the ammonium hydroxide in the aqueous solution is from 0.01 M to 1.0 M.

8 . The method of claim 1 , wherein the method further comprises combining the ammonium hexafluorosilicate and the ammonium hydroxide before adding them to the initial zeolite mixture.

9 . The method of claim 1 , wherein the ammonium hexafluorosilicate is added to the initial zeolite mixture before the ammonium hydroxide is added; or

the ammonium hydroxide is added to the initial zeolite mixture before the ammonium hexafluorosilicate is added.

10 . The method of claim 1 , wherein nothing is added to the initial zeolite mixture prior to adding the ammonium hexafluorosilicate and the ammonium hydroxide.

11 . The method of claim 1 , wherein the mesoporous zeolite has a total pore volume of at least 0.5 ml/g.

12 . The method of claim 1 , wherein the mesoporous zeolite has a total surface area of at least 650 m 2 /g.

13 . The method of claim 1 , wherein the mesoporous zeolite has a molar ratio of SiO 2 to Al 2 O 3 of from 8.5 to 15.

14 . The method of claim 1 , wherein the mesoporous zeolite comprises less than 0.05 wt. % of Na 2 O.

15 . The method of claim 1 , wherein the heating of the treated zeolite mixture is at a temperature of from 35° C. to 99° C. for from 1 hour to 24 hours.

16 . The method of claim 1 , wherein the ammonium hexafluorosilicate and the ammonium hydroxide are added to the initial zeolite mixture gradually over a period of time from 1 minute to 180 minutes.

17 . The method of claim 1 , further comprising ion-exchanging the initial zeolite prior to the combining of the initial zeolite with cetyltrimethylammonium bromide.

18 . The method of claim 1 , further comprising heating the initial zeolite mixture to a temperature of from 30° C. to 99° C. prior to adding the ammonium hexafluorosilicate and ammonium hydroxide to the initial zeolite mixture.

19 . The method of claim 1 , wherein the concentration of cetyltrimethylammonium bromide in the initial zeolite mixture is from 0.01 M to 1.0 M.

20 . The method of claim 1 , wherein the combining of the initial zeolite with the cetyltrimethylammonium bromide and the adding of the ammonium hexafluorosilicate and the ammonium hydroxide to the initial zeolite mixture occurs in a single vessel.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 16, 2023
From: ALOTAIBI, FAISAL; DING, LIANHUI
To: SAUDI ARABIAN OIL COMPANY
Reel/Frame 062719/0904 →
Continuity (1)
Related Publication 20240270583A1 · Aug 15, 2024
References Cited (16)
US 9295980B2 · Garcia-Martinez et al. · 2016 [cited by applicant]
US 9376324B2 · Senderov · 2016 [cited by examiner]
US 10407311B2 · Ding et al. · 2019 [cited by applicant]
US 20110171121A1 · Senderov et al. · 2011 [cited by applicant]
CN 107344720A · 2017 [cited by applicant]
EP 3718629A1 · 2020 [cited by applicant]
WO 2010083488A2 · 2010 [cited by applicant]
WO 2018212986A1 · 2018 [cited by applicant]
Gola et al., “Effect of leaching agent in the dealumination of stabilized Y zeolites”, Microporous and Mesoporous Materials, vol. 40, pp. 73-83, 2000. [cited by applicant]
Kerstens et al., “State of the Art and Perspectives of Hierarchical Zeolites: Practical Overview of Synthesis Methods and Use in Catalysis”, Advanced Materials, vol. 32, 2004690, 47 Pages, 2020. [cited by applicant]
Li et al., “Realizing the Commercial Potential of Hierarchical Zeolites: New Opportunities in Catalytic Cracking”, ChemCatChem, vol. 6, No. 1, pp. 46-66, 2014. [cited by applicant]
Li et al., “Defects in AHFS-dealuminated Y zeolite: A crucial factor for mesopores formation in the following base treatment procedure”, Microporous and Mesoporous Materials, vol. 255, pp. 242-252, 2018. [cited by applicant]
Martinez et al., “Stabilized hierarchical USY zeolite catalysts for simultaneous increase in diesel and LPG olefinicity during catalytic cracking”, Catalysis Science & Technology, vol. 3, pp. 972-981, 2013. [cited by applicant]
Qin et al., “Mesoporous Y zeolite with homogeneous aluminum distribution obtained by sequential desilication-dealumination and its performance in the catalytic cracking of cumene and 1,3,5-triisopropylbenzene”, Journal … [cited by applicant]
Qin et al., “A defect-based strategy for the preparation of mesoporous zeolite Y for high-performance catalytic cracking”, Journal of Catalysis, vol. 298, pp. 102-111, 2013. [cited by applicant]
Notification of Transmittal of the International Search Report and the Written Opinion of the International Searching Authority, or the Declaration dated Jun. 3, 2024 pertaining to International application No. PCT/US20… [cited by applicant]