IP Library Granted Patent US 9,670,415
Granted Patent B2
US 9,670,415 · App. 13/605,701 · Granted Jun 6, 2017

Synthesis of zeolitic materials using N,N-dimethyl organotemplates

Inventors: Bilge Yilmaz (New York, NY); Ulrich Berens (Binzen, DE); Vijay Narayanan Swaminathan (Mumbai, IN); Ulrich Müller (Neustadt, DE); Gabriele Iffland (Heidelberg, DE); Laszlo Szarvas (Ludwigshafen, DE)
Assignee: BASF SE
C10G3/49B01J29/70B01J29/7015C01B39/48C01B39/54C07C1/20C10G11/05C10G11/18C10G25/03B01D53/9413B01D53/9436B01D2255/50B01J29/85B01J29/86B01J29/87B01J2229/183C07C2529/70C10G2300/405Y02C20/10
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Quick Facts
Patent No.
US 9,670,415
App. No.
13/605,701
Granted
Jun 6, 2017
Kind
B2
Abstract

The present invention relates to a process for the preparation of a zeolitic material having a structure comprising YO 2 and optionally comprising X 2 O 3 , preferably comprising YO 2 and X 2 O 3 , wherein said process comprises the steps of (1) providing a mixture comprising one or more ammonium compounds of which the ammonium cation has the formula (I): [R 1 R 2 NR 3 R 4 ] +   (I) and further comprising one or more sources for YO 2 and one or more sources for X 2 O 3 ; (2) crystallizing the mixture provided in (1); wherein Y is a tetravalent element, and X is a trivalent element, and wherein in formula (I) R 1 and R 2 are independently from one another derivatized or underivatized methyl, and R 3 and R 4 are independently from one another derivatized or underivatized (C 3 -C 5 )alkyl, and wherein the molar ratio of ammonium cation having the formula (I) to Y in the mixture provided in step (1) and crystallized in step (2) is equal to or greater than 0.25.

Claims (48)

1. A process for the preparation of a zeolitic material having a CHA framework structure wherein said process comprises

(1) providing a mixture comprising

N,N-dimethylpiperidinium hydroxide, and

one of more sources for YO 2 and one or more sources for X 2 O 3 ;

(2) crystallizing the mixture provided in (1);

wherein Y is a tetravalent element, and X is a trivalent element, and

wherein the molar ratio of ammonium cation having the formula (I) to Y in the mixture provided in (1) and crystallized in (2) is equal to or greater than 0.25;

wherein the zeolitic material comprises YO 2 and X 2 O 3 wherein Y is a tetravalent element, and X is a trivalent element, and

wherein the zeolitic material displays a Y:X molar ratio in the range of from 1.5 to 10.5,

wherein the zeolitic material optionally further comprises Z 2 O 5 in addition to YO 2 and X 2 O 3 , wherein Z is a pentavalent element, and

wherein the zeolitic material then displays a Y:nX:pZ molar ratio, the value for the ratio (1+2p):(n−p) is in the range of from 1 to 5.5.

2. The process of claim 1 , wherein Y is selected from the group consisting of Si, Sn, Ti, Zr, Ge, and mixtures of two or more thereof.

3. The process of claim 1 , wherein the one or more sources for YO 2 comprises one or more compounds selected from the group consisting of silicas, fumed silicas, silicates, and mixtures of two or more thereof.

4. The process of claim 1 , wherein X is selected from the group consisting of Al, B, In, Ga, and mixtures of two or more thereof.

5. The process of claim 1 , wherein the one or more sources for X 2 O 3 comprises one or more compounds selected from the group consisting of aluminas, aluminates, and mixtures of two or more thereof.

6. The process of claim 1 , wherein the structure of the zeolitic material further comprises Z 2 O 5 in addition to YO 2 and X 2 O 3 , and wherein the mixture provided in (1) further comprises one or more sources for Z 2 O 5 , wherein Z is a pentavalent element.

7. The process of claim 6 , wherein Z is selected from the group consisting of P, As, Sb, Bi, V, Nb, Ta, and mixtures of two or more thereof.

8. The process of claim 1 , wherein the mixture provided in step (1) further comprises a solvent.

9. The process of claim 8 , wherein the solvent comprises water, and wherein the H 2 O:YO 2 molar ratio of the mixture provided in (1) ranges from 1 to 150 and

wherein the H 2 O:X 2 O 3 molar ratio of the mixture provided in (1) ranges from 100 to 8,000.

10. The process of claim 8 , wherein the solvent comprises water, and wherein the pH of the mixture provided in (1) is in the range of from 8 to 14.

11. The process of claim 1 , wherein the crystallization in step (2) involves heating of the mixture.

12. The process of claim 11 , wherein the heating in step (2) is conducted under solvothermal conditions.

13. The process of claim 11 , wherein the crystallization in (2) involves heating of the mixture for a period ranging from 0.1 to 20 d.

14. The process of claim 1 , further comprising one or more of

(3) isolating the zeolitic material, preferably by filtration,

and/or

(4) washing the zeolitic material,

and/or

(5) drying the zeolitic material.

15. The process of claim 14 , further comprising one or more of

(6) calcining the zeolitic material obtained according to (2) or (3) or (4) or (5),

wherein the steps (3) and/or (4) and/or (5) and/or (6) can be conducted in any order.

16. A synthetic zeolitic material having a CHA framework structure, said zeolitic material being optionally obtainable and/or obtained by a process comprising

(1) providing a mixture comprising N,N-dimethylpiperidinium hydroxide

and one or more sources for YO 2 and one or more sources for X 2 O 3 ;

(2) crystallizing the mixture provided in (1);

wherein Y is a tetravalent element, and X is a trivalent element,

wherein the molar ratio of ammonium cation having the formula (I) to Y in the mixture provided in (1) and crystallized in (2) is equal to or greater than 0.25,

wherein the zeolitic material comprises YO 2 and X 2 O 3 , wherein Y is a tetravalent element and X is a trivalent element, and

wherein the zeolitic material displays a Y:X molar ratio comprised in the range of from 1.5 to 10.5,

wherein when the zeolitic material optionally further comprises Z 2 O 5 in addition to YO 2 and X 2 O 3 , wherein Z is a pentavalent element, and

wherein the zeolitic material then displays a Y:nX:pZ molar ratio, the value for the ratio (1+2p):(n−p) is in the range of from 1 to 5.5.

17. The synthetic zeolitic material of claim 16 , wherein the material comprises one or more zeolites selected from the group consisting of (Ni(deta) 2 )-UT-6, Chabazite, |Li—Na|[Al—Si—O]-CHA, DAF-5, Dehyd. Na-Chabazite, K-Chabazite (Iran), LZ-218, Linde D, Linde R, MeAPSO-47, Phi, SAPO-34, SAPO-47, SSZ-13, SSZ-62, UiO-21, Willhendersonite, ZK-14, ZYT-6, and combinations of two or more thereof.

18. The material of claim 16 , wherein Z is selected from the group consisting of P, As, Sb, Bi, V, Nb, Ta, and mixtures of two or more thereof.

19. The material of claim 16 , wherein the framework structure does not contain a pentavalent element Z in addition to YO 2 and X 2 O 3 .

20. The material of claim 16 , wherein Y is selected from the group consisting of Si, Sn, Ti, Zr, Ge, and mixtures of two or more thereof.

21. The material of claim 16 , wherein X is selected from the group consisting of Al, B, In, Ga, and mixtures of two or more thereof.

Assignments (3)
NUNC PRO TUNC ASSIGNMENT Recorded Jan 24, 2025
From: BASF SE
To: BASF CATALYSTS LLC
Reel/Frame 070001/0877 →
NUNC PRO TUNC ASSIGNMENT Recorded Jan 24, 2025
From: BASF CATALYSTS LLC
To: BASF MOBILE EMISSIONS CATALYSTS LLC
Reel/Frame 070002/0453 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 7, 2012
From: YILMAZ, BILGE; BERENS, ULRICH; SWAMINATHAN, VIJAY NARAYANAN; MUELLER, ULRICH; IFFLAND, GABRIELE; SZARVAS, LASZLO
To: BASF SE
Reel/Frame 028918/0587 →
Continuity (2)
Provisional Application 61531102 · Sep 6, 2011
Related Publication 20130059723A1 · Mar 7, 2013