Method of preparing hydrocarbon aromatization catalyst, the catalyst, and the use of the catalyst
US-9782758-B2 · Oct 10, 2017 · US
US10427141B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10427141-B2 |
| Application number | US-201816178645-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 2, 2018 |
| Priority date | Nov 22, 2013 |
| Publication date | Oct 1, 2019 |
| Grant date | Oct 1, 2019 |
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In an embodiment, A catalyst comprises a zeolite comprising Si, Al, and Ge in the framework with Pt deposited thereon; wherein the catalyst has an Si:Al2 mole ratio of greater than or equal to 125, an Si:Ge mole ratio of 40 to 400, and an Na:Al mole ratio of 0.9 to 2.5; wherein the catalyst has an aluminum content of less than or equal to 0.75 wt %; wherein the catalyst is non-acidic.
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The invention claimed is: 1. A catalyst comprising: a zeolite comprising Si, Al, and Ge in the framework with Pt deposited thereon; wherein the zeolite is a medium pore zeolite having an average pore size of 5 to 8 Å; wherein the zeolite further comprises Na; wherein the catalyst has an Si:Al 2 mole ratio of 125 to 211, an Si:Ge mole ratio of 40 to 400, and an Na:Al mole ratio of 0.9 to 2.5; wherein the catalyst has an aluminum content of less than or equal to 0.75 wt %, and a Ge content of 0.1 to 3 wt %, based on the total weight of the catalyst excluding any binder and extrusion aide; wherein the catalyst is non-acidic. 2. The catalyst of claim 1 , wherein the Ge is present in an amount of 0.4 to 2.5 wt %, and/or the Na is present in an amount of 0.5 to 2 wt % and/or the Pt is present in an amount of 0.05 to 3 wt %, wherein the wt % values are based on the total weight of the catalyst excluding any binder and extrusion aide. 3. The catalyst of claim 2 , wherein the Ge content of 0.4 to 2.5 wt %, the Na content of 0.5 to 2 wt %, and the Pt content of 0.05 to 3 wt %, wherein the wt % values are based on the total weight of the catalyst excluding any binder and extrusion aide. 4. The catalyst of claim 1 , wherein the catalyst has a Ge content of 0.4 to 1.5 wt % based on the total weight of the catalyst excluding any binder and extrusion aide. 5. The catalyst of claim 1 , wherein the catalyst comprises Al in an amount of 0.45 to 0.7 wt % based on the total weight of the catalyst excluding any binder and extrusion aide. 6. The catalyst of claim 1 , wherein the zeolite is a ZSM-5 zeolite. 7. The catalyst of claim 1 , wherein the Si:Ge mole ratio of 50 to 300. 8. The catalyst of claim 1 , wherein the Na:Al mole ratio of 1.2 to 2.2. 9. The catalyst of claim 1 , wherein the Si:Al 2 mole ratio is 125 to 200. 10. A method for the aromatization of hydrocarbons comprising contacting an alkane containing 6 to 12 carbon atoms per molecule with the catalyst of claim 1 . 11. A catalyst comprising: a zeolite comprising Si, Al, and Ge in the framework with Pt deposited thereon; wherein the zeolite further comprises Na; wherein the catalyst has an Si:Al 2 mole ratio of greater than or equal to 125, an Si:Ge mole ratio of 40 to 400, and an Na:Al mole ratio of 0.9 to 2.5; wherein the catalyst has an aluminum content of less than or equal to 0.75 wt %; wherein the catalyst is non-acidic. 12. The catalyst of claim 11 , wherein the zeolite is a medium pore zeolite having an average pore size of 5 to 8 Å. 13. The catalyst of claim 11 , wherein the Si:Al 2 mole ratio of 125 to 211. 14. The catalyst of claim 11 , wherein the catalyst has a Ge content of 0.1 to 3 wt % based on the total weight of the catalyst excluding any binder and extrusion aide. 15. A method for the aromatization of hydrocarbons comprising contacting an olefin with the catalyst of claim 1 . 16. The method of claim 15 , wherein the Ge is present in an amount of 0.3 to 3 wt %, and/or the Na is present in an amount of 0.5 to 2 wt % and/or the Pt is present in an amount of 0.05 to 3 wt %, wherein the wt % values are based on the total weight of the final catalyst excluding any binder and extrusion aide.
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