Process for the preparation of zeolites having CHA structure
Zeolites having CHA framework structure and a composition comprising the molar ratio (n SiO2): X203, wherein X is a trivalent element, and wherein n is at least 10, wherein the crystal size, as determined from Scanning Electron Microscopy, is greater than 1 micrometer and wherein the chabazite framework is phase-pure having an impurity of other zeolitic frameworks, such as RUT 25 as determined by X-ray Diffraction, of less than 5%. The process for the preparation comprises: (i) preparation of an aqueous solution containing at least one source for X203 , wherein X is selected from Al, B, Ga, and a mixture of two or more, and at least one source for SiO2, at least one organic structure directing agent (SDA) other than Tetramethylammonium hydroxide (TMAOH), acting as a template for the CHA structure, and Tetramethylammonium hydroxide (TMAOH), wherein the SDA or mixtures thereof are employed in such amounts that the aqueous solution in (i) exhibits a molar ratio of SDA : TMAOH of 0.01 to 5; (ii) hydrothermal crystallization of the aqueous solution according to (i); wherein the aqueous solution of (i) contains copper in an amount less than 0.005 Cu:((n YO2)+X203) where n is in the range of 10 to 50.
1. A zeolitic material having framework structure CHA, having a composition comprising the molar ratio (n SiO 2 ):X 2 O 3 , wherein X is a trivalent element, and wherein X is selected from Al, B, Ga, and a mixture of two or more, and n is at least 10, obtainable by a process comprising:
(i) preparation of an aqueous solution containing:
at least one source for X 2 O 3 , wherein X is selected from Al, B, Ga, and a mixture of two or more,
at least one source for SiO 2 ,
at least one organic structure directing agent (SDA) other than Tetramethylammonium hydroxide (TMAOH) as a template for the CHA structure, and
Tetramethylammonium hydroxide (TMAOH),
wherein the SDA or mixtures thereof are employed in such amounts that the aqueous solution in (i) exhibits a molar ratio of SDA:TMAOH in the range of 0.01 to 5;
(ii) hydrothermal crystallization of the aqueous solution according to (i);
wherein the aqueous solution of (i) contains copper in an amount less than 0.005 Cu: ((n SiO 2 )+X 2 O 3 ) where n is at least 10, and
wherein the zeolitic material having framework structure CHA has a sodium content of 1000 ppm or less.
2. A method for the selective reduction (SCR) of nitrogen oxides NO x , for the oxidation of NH 3 or for the decomposition of N 2 O, the method comprising contacting a stream comprising NOx, NH 3 or N 2 O with a catalyst comprising the zeolitic material of claim 1 .
3. A method for catalyzing a chemical reaction, the method comprising using the zeolitic material of claim 1 as a catalytically active material in a chemical reaction.
4. A catalyst comprising the zeolitic material of claim claim 1 .
5. The zeolitic material of claim 1 , wherein the aqueous solution obtained in (i) and subjected to hydrothermal crystallization in (ii) is free of sodium.
6. The zeolitic material of claim 1 , wherein the aqueous solution obtained in (i) and subjected to hydrothermal crystallization in (ii) has a sodium content of 1000 ppm or less.
7. The zeolitic material of claim 1 , wherein the zeolitic material is free of sodium.
8. A zeolitic material having framework structure CHA, having a composition comprising the molar ratio (n SiO 2 ):X 2 O 3 , wherein X is a trivalent element, and wherein X is selected from Al, B, Ga, and a mixture of two or more, and n is at least 10, and wherein the crystal size of that zeolitic material, as determined from Scanning Electron Microscopy, is greater than 1 micrometer and wherein the chabazite framework is phase-pure having an impurity of other zeolitic frameworks of less than 5%, as determined by X-ray Diffraction, and
wherein the zeolitic material having framework structure CHA has a sodium content of 1000 ppm or less.
9. The zeolitic material of claim 8 , wherein the crystal size is in the range of greater than 1 micron to 5 microns.
10. The zeolitic material of claim 8 , wherein the chabazite framework is phase-pure having an impurity of other zeolitic frameworks of less than 1%.
11. A method for the selective reduction (SCR) of nitrogen oxides NO x , for the oxidation of NH 3 or for the decomposition of N 2 O, the method comprising contacting a stream comprising NOx, NH 3 or N 2 O with a catalyst comprising the zeolitic material of claim 8 .
12. A method for catalyzing a chemical reaction, the method comprising using the zeolitic material of claim 8 as a catalytically active material in a chemical reaction.
13. A catalyst comprising the zeolitic material of claim claim 8 .
14. The zeolitic material of claim 8 , wherein the zeolitic material is free of sodium.