IP Library › Granted Patent US 12,606,449
Granted Patent B2
US 12,606,449 · App. 18/325,342 · Granted Apr 21, 2026

Molecular sieve SSZ-117x with high acidity

Inventor: Stacey I. Zones (San Francisco, CA)
C01B39/48B01J29/047B01J29/70C01B39/06C01P2002/72
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 12,606,449
App. No.
18/325,342
Granted
Apr 21, 2026
Kind
B2
Abstract

A novel synthetic crystalline aluminogermanosilicate molecular sieve material, designated SSZ-117x, is provided which exhibits increased acidity. The SSZ-117x can be synthesized using N,N,N,3,5-pentamethyladamantan-1-ammonium cations as a structure directing agent. The synthesis employs a boron pathway to achieve increased acid sites. The SSZ-117x of increased acidity may be used in organic compound conversion reactions and/or sorptive processes.

Claims (78)

1 . A molecular sieve having a powder X-ray diffraction pattern including the following peaks:

2-Theta

d-Spacing, nm

Relative Intensity

8.00

1.10

M

11.65

0.76

VS

18.8

0.47

M

21.8

0.41

M(Broad)

22.8

0.39

S

and with the molecular sieve comprising boron and having increased acid sites due to a boron pathway.

2 . The molecular sieve of claim 1 , having a composition comprising a molar relationship:

Al 2 O 3 :( n )TO 2

wherein n is ≥150; and T is a tetravalent element comprising silicon and germanium.

3 . The molecular sieve of claim 1 , having a composition comprising a molar relationship:

Al 2 O 3 :( n )TO 2

wherein n is ≥300; and T is a tetravalent element comprising silicon and germanium.

4 . The molecular sieve of claim 1 , having a chemical composition comprising the following molar relationship:

TO 2 /Al 2 O 3

≥150

SiO 2 /GeO 2

4 to 12

wherein T is a tetravalent element comprising silicon and germanium.

5 . A process for converting a feedstock comprising an organic compound to a conversion product, the process comprising contacting the feedstock at organic compound conversion conditions with a catalyst comprising the molecular sieve of claim 4 .

6 . A process of ion exchanging metals, the process comprising contacting a stream comprising heavy metals with the molecular sieve of claim 4 .

7 . The molecular sieve of claim 1 , wherein the amount of boron in the molecular sieve ranges from 50-250 ppm.

8 . A method of synthesizing the molecular sieve of claim 1 , the method comprising:

(a) providing a reaction mixture comprising:

(1) a FAU framework type zeolite having a SiO 2 /Al 2 O 3 mol ratio of 300 or greater;

(2) a source of germanium;

(3) a source of boron;

(4) N,N,N,3,5-pentamethyladamantan-1-ammonium hydroxide (Q);

(5) a source of fluoride ions; and

(6) water;

(b) subjecting the reaction mixture to crystallization conditions sufficient to form crystals of the molecular sieve which contain boron;

(c) removing Q from the molecular sieve framework; and

(d) replacing some of the boron in the molecular sieve crystals with aluminum.

9 . The method of claim 8 , wherein the reaction mixture has a composition, in terms of molar ratios, as follows:

TO 2 /B 2 O 3

≥10

Q/TO 2

0.10 to 1.00

F/TO 2

0.10 to 1.00

H 2 O/TO 2

2 to 10

SiO 2 /GeO 2

4 to 12

wherein T is a tetravalent element comprising silicon and germanium.

10 . The method of claim 8 , wherein the reaction mixture has a composition, in terms of molar ratios, as follows:

TO 2 /B 2 O 3

15 to 20

Q/TO 2

0.20 to 0.70

F/TO 2

0.20 to 0.70

H 2 O/TO 2

4 to 8

SiO 2 /GeO 2

7 to 10

wherein T is a tetravalent element comprising silicon and germanium.

11 . The method of claim 8 , wherein the FAU framework type zeolite is zeolite Y, or a post-synthetic modified form.

12 . The method of claim 8 , wherein the crystallization conditions include a temperature of from 125° C. to 200° C.

13 . The method of claim 8 , wherein the reaction mixture has a Q/F molar ratio in a range of 0.8 to 1.2.

14 . The process of claim 8 , wherein the Q is removed by calcination.

15 . The process of claim 8 , wherein the Q is removed by treatment with ozone.

16 . The process of claim 8 , wherein the replacing of boron with aluminum comprises refluxing the molecular sieve crystals with a solution of aluminum nitrate.

17 . A process for converting a feedstock comprising an organic compound to a conversion product, the process comprising contacting the feedstock at organic compound conversion conditions with a catalyst comprising the molecular sieve of claim 1 .

18 . A process of ion exchanging metals, the process comprising contacting a stream comprising heavy metals with the molecular sieve of claim 1 .

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 6, 2024
From: ZONES, STACEY I.
To: CHEVRON U.S.A. INC.
Reel/Frame 066392/0549 →
Continuity (2)
Provisional Application 63365514 · May 31, 2022
Related Publication 20230382748A1 · Nov 30, 2023
References Cited (15)
US 11161750B1 · Zones · 2021 [cited by applicant]
US 20050087478A1 · Zones · 2005 [cited by examiner]
US 20050194289A1 · Overbeek et al. · 2005 [cited by applicant]
US 20060115417A1 · Yuen et al. · 2006 [cited by applicant]
US 20080058196A1 · Zones et al. · 2008 [cited by applicant]
US 20110318263A1 · Zones et al. · 2011 [cited by applicant]
US 20150011787A1 · Bellussi et al. · 2015 [cited by applicant]
US 20170128923A1 · Yang et al. · 2017 [cited by applicant]
US 20190256364A1 · Zones et al. · 2019 [cited by applicant]
US 20190375648A1 · Xie et al. · 2019 [cited by applicant]
US 20210221696A1 · Zones et al. · 2021 [cited by applicant]
US 20220072520A1 · Zones et al. · 2022 [cited by applicant]
CN 113343948A · 2021 [cited by applicant]
WO 2021082140A1 · 2021 [cited by applicant]
International Search Report and Written Opinion from PCT/US2023/067601 mailed Oct. 4, 2023. [cited by applicant]