CHA-type zeolite materials and methods for their preparation using cycloalkyammonium compounds

Patent metadata

Field	Value
Publication number	US-9636667-B2
Application number	US-201313908666-A
Country	US
Kind code	B2
Filing date	Jun 3, 2013
Priority date	Jun 4, 2012
Publication date	May 2, 2017
Grant date	May 2, 2017

Abstract

Aspects of the present invention relate to a process for the preparation of a zeolitic material having a CHA-type framework structure comprising YO 2 and X 2 O 3 , wherein said process comprises the steps of:
(1) providing a mixture comprising one or more sources for YO 2 , one or more sources for X 2 O 3 , and one or more tetraalkylammonium cation R 1 R 2 R 3 R 4 N + -containing compounds as structure directing agent; (2) crystallizing the mixture obtained in step (1) for obtaining a zeolitic material having a CHA-type framework structure;

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

wherein R 1 , R 2 , and R 3 independently from one another stand for alkyl,

wherein R 4 stands for cycloalkyl, and

wherein the mixture provided in step (1) does not contain any substantial amount of a source for Z 2 O 5 , wherein Z is P, as well as to zeolitic materials which may be obtained according to the inventive process and to their use.

First claim

The invention claimed is:

1. A process for the preparation of a zeolitic material having a CHA-type framework structure comprising YO 2 and X 2 O 3 , wherein said process comprises the steps of:
(1) providing a mixture comprising one or more sources for YO 2 , one or more sources for X 2 O 3 , and one or more tetraalkylammonium cation R 1 R 2 R 3 R 4 N + -containing compounds as structure directing agent;
(2) crystallizing the mixture obtained in step (1) for obtaining a zeolitic material having a CHA-type framework structure;

wherein Y is a tetravalent element and X is a trivalent element,
wherein the mixture provided in step (1) further comprises seed crystals,
wherein R 1 , R 2 , and R 3 independently from one another stand for alkyl,
wherein R 4 stands for cycloalkyl, and
wherein the mixture provided in step (1) does not contain any substantial amount of a source for Z 2 O 5 , wherein Z is P, and wherein the one or more tetraalkylammonium cation R 1 R 2 R 3 R 4 N + -containing compounds comprises one or more N,N,N-trimethyl-cyclohexylammonium compounds.

2. The process of claim 1 , wherein the one or more N,N,N-trimethyl-cyclohexylammonium containing compounds are salts.

3. 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.

4. 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 fumed silica, silica hydrosols, reactive amorphous solid silicas, silica gel, silicic acid, water glass, sodium metasilicate hydrate, sesquisilicate, disilicate, colloidal silica, silicic acid esters, and mixtures of two or more thereof.

5. 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.

6. 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 alumina, aluminates, aluminum salts, and mixtures of two or more thereof.

7. The process of claim 1 , wherein the YO 2 : X 2 O 3 molar ratio of the mixture according to step (1) ranges from 0.5 to 500.

8. The process of claim 1 , wherein the mixture according to step (1) further comprises one or more solvents.

9. The process of claim 1 , wherein the H 2 O:YO 2 molar ratio of the mixture according to step (1) ranges from 3 to 50.

10. The process of claim 1 , wherein the molar ratio of the one or more N,N,N-trimethyl-cyclohexylammonium cations: YO 2 in the mixture provide according to step (1) ranges from 0.05 to 3.

11. The process of claim 1 , wherein the mixture provided in step (1) contains 3 wt.-% or less of one or more metals M based on 100 wt-% of YO 2 , wherein M stands for sodium or potassium.

12. The process of claim 1 , wherein the mixture according to step (1) further comprises one or more sources of one or more elements suitable for isomorphous substitution of at least a portion of the Y atoms and/or of the X atoms in the CHA-type framework structure.

13. The process of claim 1 , wherein the molar ratio of YO 2 to the one or more elements suitable for isomorphous substitution ranges from 5 to 200.

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

15. The process of claim 1 , wherein the crystallization in step (2) is conducted under solvothermal conditions.

16. The process of claim 1 , wherein the crystallization in step (2) involves heating of the mixture for a period ranging from 0.5 to 50 d.

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

18. The process of claim 1 , further comprising one or more of the following steps of
(3) isolating the zeolitic material,
and/or
(4) washing the zeolitic material,
and/or
(5) drying the zeolitic material,
and/or
(6) subjecting the zeolitic material to an ion-exchange procedure,
wherein the steps (3) and/or (4) and/or (5) and/or (6) can be conducted in any order.

19. The process of claim 18 , wherein in the at least one step (6) one or more ionic non-framework elements contained in the zeolite framework is ion-exchanged.

20. The process of claim 1 , wherein the amount of seed crystals in the mixture according to step (1) ranges from 0.1 to 20 wt.-% based on 100 wt.-% of YO 2 in the at least one source for YO 2 .

21. The process of claim 1 , wherein the mixture provided in step (1) does not contain any substantial amount of a trimethyl benzyl ammonium containing compound.

22. A synthetic zeolitic material having a CHA-type framework structure obtainable and/or obtained according to claim 1 , wherein the CHA-type framework structure comprises YO 2 and X 2 O 3 , wherein the CHA-type framework does not contain any substantial amount of P and/or As.

23. The zeolitic material of claim 22 , wherein the 27 Al MAS NMR of the untreated zeolitic material as-synthesized comprises:
a first peak (P 1 ) in the range of from 52.3 to 58.6 ppm; and
a second peak (P 2 ) in the range of from −2.3 to −4.1 ppm; wherein the integration of the first and second peaks in the 27 Al MAS NMR of the zeolitic material offers a ratio of the integration values P 1 :P 2 comprised in the range of from 1: (0-0.22).

24. The zeolitic material of claim 22 , wherein the IR-spectrum of the zeolitic material comprises:
a first absorption band (B 1 ) in the range of from 3,550 to 3,660 cm −1 ; and
a second absorption band (B 2 ) in the range of from 1,800 to 1,930 cm-1;

wherein the ratio of the maximum absorbance of the first absorption band to the second absorption band B 1 : B 2 is comprised in the range of from 3.0 to 5.2.

25. The zeolitic material of claim 24 , wherein the IR-spectrum of the zeolitic material further comprises:
a third absorption band (B 3 ) in the range of from 3,665 to 3,730 cm −1 ; and
a fourth absorption band (B 4 ) in the range of from 3,450 to 3,545 cm −1 ;

wherein the ratio of the maximum absorbance of the third absorption band to the second absorption band B 3 : B 2 is comprised in the range of from 1.5 to 3.5; and
wherein the ratio of the maximum absorbance of the fourth absorption band to the second absorption band B 4 : B 2 is comprised in the range of from 1.6 to 3.6.

26. The zeolitic material of claim 22 , wherein the IR-spectrum of the zeolitic material further comprises:
a first absorption band (B′ 1 ) in the range of from 3,550 to 3,660 cm −1 ;
a second absorption band (B′ 2 ) in the range of from 3,450 to 3,545 cm −1 ;
a third absorption band (B′ 3 ) in the range of from 1,800 to 1,930 cm −1 ;

wherein the ratio of the maximum absorbance of the first absorption band to the third absorption band B′ 1 : B′ 3 is comprised in the range of from 0.30 to 2.5; and
wherein the ratio of the maximum absorbance of the second absorption band to the third absorption band B′ 2 : B′ 3 is comprised in the range of from 0.1 to 3.0.

27. The zeolitic material of claim 22 , wherein the YO 2 : X 2 O 3 molar ratio ranges from 2 to 200.

28. The zeolitic material of claim 22 , wherein Y is selected from the group consisting of Si, Sn, Ti, Zr, Ge, and mixtures of two or more thereof.

29. The zeolitic material of claim 22 , wherein X is selected from the grou

Assignees

• Basf Se

Inventors

• Feyen Mathias
• Müller Ulrich
• Ruetz Roger
• Bein Thomas
• Möller Karin

Classifications

• B01D53/565

  by treating the gases with solids · CPC title

• B01J29/7015 Primary

  CHA-type, e.g. Chabazite, LZ-218 · CPC title

• Y02P20/153

  Cross-Sectional Technologies · mapped topic

• B01J29/67

  Noble metals · CPC title

• B01D2258/012

  Diesel engines and lean burn gasoline engines · CPC title