Process for preparing a titanium-containing zeolitic material having an mww framework structure
US-2015368115-A1 · Dec 24, 2015 · US
US9895684B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9895684-B2 |
| Application number | US-201414534642-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 6, 2014 |
| Priority date | Nov 24, 2009 |
| Publication date | Feb 20, 2018 |
| Grant date | Feb 20, 2018 |
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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.
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The invention claimed is: 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.
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