Method of producing propylene and ethylene with a core-shell ZSM catalyst
US-10016750-B1 · Jul 10, 2018 · US
US12102986B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12102986-B2 |
| Application number | US-202217838063-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 10, 2022 |
| Priority date | Jul 15, 2021 |
| Publication date | Oct 1, 2024 |
| Grant date | Oct 1, 2024 |
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A de-hydrogenation catalyst and its use in dehydrogenation of hydrocarbons. The catalyst has low cracking activity and comprises gallium or gallium and platinum on an essentially non-acidic and amorphous alumina-phosphate or silica-alumina-phosphate support with an empirical chemical composition of [Al2O3][SiO2]Y[P2O5]Z, wherein Y is between 0 and 0.2 and Z is between 0.01 and 1.1, with a BET surface area above 50 m2/g, as measured by N2 adsorption experiment.
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The invention claimed is: 1. A de-hydrogenation catalyst comprising gallium on an essentially non-acidic and amorphous alumina-phosphate or silica-alumina-phosphate support with an empirical chemical composition of [Al2O3][SiO2]Y[P2O5] Z , wherein Y is between 0 and 0.2 and Z is between 0.01 and 1.1, with a BET surface area above 50 m 2 /g, as measured by N 2 adsorption experiment. 2. The catalyst of claim 1 further comprising platinum. 3. The catalyst of claim 2 comprising 1 to 500 ppm by weight platinum. 4. The catalyst of claim 2 comprising about 0.25 to 1.5 wt % gallium and about 20 ppm to 100 ppm by weight platinum. 5. The catalyst of claim 2 with an atomic ratio of Ga/Pt between 140 and 4500. 6. The catalyst of claim 2 having an atomic ratio of Ga/Pt between 200 and 500. 7. A method of preparing the catalyst of claim 2 comprising impregnating an alumina-phosphate or a silica-alumina-phosphate support with a solution containing gallium and platinum. 8. The method of claim 7 further comprising calcining the catalyst in wet or dry air at a temperature of about 600° C. to 900° C. 9. A method of preparing the catalyst of claim 2 comprising separate steps of impregnating a gallium containing solution and a platinum containing solution on the alumina-phosphate or silica-alumina-phosphate support. 10. The catalyst of claim 1 comprising 0.05-2.5 wt % gallium. 11. A process for dehydrogenating a hydrocarbon comprising: contacting a gaseous stream consisting of at least one dehydrogenatable hydrocarbon selected from paraffinic hydrocarbons having from 2 to 20 carbons, alkylaromatic hydrocarbons having from 8 to 20 carbons, and mixtures thereof, hydrogen produced in situ by the dehydrogenation and a carrier fluid selected from the group consisting of one of the reactants in gaseous form, nitrogen, hydrocarbons, carbon dioxide, and argon; or at least one dehydrogenatable hydrocarbon selected from paraffinic hydrocarbons having from 2 to 20 carbons, alkylaromatic hydrocarbons having from 8 to 20 carbons, and mixtures thereof and hydrogen produced in situ by the dehydrogenation, in a dehydrogenation reactor with a supported dehydrogenation catalyst comprising gallium on an essentially non-acidic and amorphous alumina-phosphate or silica-alumina-phosphate support with the empirical chemical composition of [Al2O3][SiO2]Y[P2O5] Z , in which Y is between 0 and 0.2 and Z is between 0.01 and 1.1, with a BET surface area above 50 m 2 /g, as measured by N 2 adsorption experiment. 12. The process of claim 11 wherein said supported dehydrogenation catalyst further comprises platinum. 13. The process of claim 11 wherein said supported dehydrogenation catalyst comprises 0.05-2.5 wt % gallium. 14. The process of claim 11 wherein said supported dehydrogenation catalyst comprises 1 to 500 ppm by weight platinum. 15. The process of claim 11 wherein the dehydrogenation operates at a temperature of from 400° to about 900° C. 16. The process of claim 11 wherein the dehydrogenation operates at a pressure of 0.01 to 10 atmospheres.
10-100 m2/g · CPC title
Metals, or metals deposited on a carrier · CPC title
Aromatics or polyaromatics · CPC title
Platinum · CPC title
Gallium · CPC title
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