Post-treatment of deboronated zeolite beta
US-2015344317-A1 · Dec 3, 2015 · US
US11142464B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11142464-B2 |
| Application number | US-201816758200-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 25, 2018 |
| Priority date | Oct 25, 2017 |
| Publication date | Oct 12, 2021 |
| Grant date | Oct 12, 2021 |
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Provided is a beta zeolite also having exceptional catalytic activity as a catalyst other than an olefin epoxidation catalyst. This beta zeolite is synthesized without using an organic structure-directing agent and has titanium in the structural skeleton thereof, the Ti content being 0.10 mmol/g or higher. This beta zeolite preferably has an Si/Ti molar ratio of 20-200. Also, the Si/Al molar ratio is preferably 100 or higher.
Opening claim text (preview).
The invention claimed is: 1. A beta zeolite comprising a titanium-containing structural skeleton and having a Ti content of 0.10 mmol/g or more, the beta zeolite being synthesized without using any organic structure-directing agent, wherein the beta zeolite has a nitrogen adsorption isotherm at −196° C. that shows a nitrogen absorption of 100 to 175 cm 3 (STP)/g at a relative pressure P/P 0 of 0.4 and shows a nitrogen absorption of 160 to 220 cm 3 (STP)/g at a relative pressure P/P 0 of 0.9, in which P and P 0 are respectively the equilibrium pressure and the saturated vapor pressure at a temperature of −196° C. 2. The beta zeolite according to claim 1 , which has a Si/Ti molar ratio of 20 or more and 200 or less. 3. The beta zeolite according to claim 1 , which has a Si/Al molar ratio of 100 or more. 4. An oxidation catalyst comprising the beta zeolite according to claim 1 and being for use in oxidation of phenols. 5. An olefin epoxidation catalyst comprising the beta zeolite according to claim 1 . 6. A method for producing the beta zeolite according to claim 1 , comprising: performing ion exchange on a raw material beta zeolite synthesized without using any organic structure-directing agent to form an ammonium-type beta zeolite; then exposing the ammonium-type beta zeolite to water vapor; performing an acid treatment on the beta zeolite after the exposure; and then introducing Ti into the beta zeolite after the acid treatment. 7. The method for producing the beta zeolite according to claim 6 , wherein the Ti is introduced by treating the beta zeolite with a gaseous form of titanium chloride after the acid treatment. 8. The method for producing the beta zeolite according to claim 6 , wherein the acid treatment is performed to increase a Si/Al molar ratio of the beta zeolite to 300 or more after the exposure to water vapor. 9. A method for oxidation of phenol, comprising oxidizing the phenol using the oxidation catalyst according to claim 4 with an alcohol.
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