Catalyst and method for preparing light olefins by direct conversion of syngas
US-11084026-B2 · Aug 10, 2021 · US
US11986799B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11986799-B2 |
| Application number | US-201917417846-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 16, 2019 |
| Priority date | Dec 28, 2018 |
| Publication date | May 21, 2024 |
| Grant date | May 21, 2024 |
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A process for preparing C 2 to C 4 olefins includes introducing a feed stream comprising hydrogen gas and a carbon-containing gas selected from carbon monoxide, carbon dioxide, and mixtures thereof into a reaction zone of a reactor. The feed stream is converted into a product stream including C 2 to C 4 olefins in the reaction zone in the presence of the hybrid catalyst. The hybrid catalyst includes a metal oxide catalyst component comprising gallium oxide and phase pure zirconia, and a microporous catalyst component.
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The invention claimed is: 1. A process for preparing C 2 to C 4 olefins comprising: introducing a feed stream comprising hydrogen gas and a carbon-containing gas selected from the group consisting of carbon monoxide, carbon dioxide, and mixtures thereof into a reaction zone of a reactor; and converting the feed stream into a product stream comprising C 2 to C 4 olefins in the reaction zone in the presence of a hybrid catalyst, the hybrid catalyst comprising: a metal oxide catalyst component comprising gallium oxide and phase pure zirconia; and a microporous catalyst component. 2. The process of claim 1 , wherein the phase pure zirconia comprises crystalline phase pure zirconia. 3. The process of claim 1 , wherein the phase pure zirconia comprises monoclinic phase pure zirconia. 4. The process of claim 1 , wherein the phase pure zirconia has a BET surface area that is greater than or equal to 40 m 2 /g. 5. The process of claim 1 , wherein the phase pure zirconia has a BET surface area that is greater than or equal to 100 m 2 /g. 6. The process of claim 1 , wherein the metal oxide catalyst component comprises from greater than 0.0 g gallium per 100 g phase pure zirconia to 30.0 g gallium per 100 g of phase pure zirconia. 7. The process of claim 1 , wherein the metal oxide catalyst component comprises from greater than 0.0 g gallium per 100 g phase pure zirconia to 15.0 g gallium per 100 g of phase pure zirconia. 8. The process of claim 1 , wherein microporous catalyst component comprises an 8 membered ring structure. 9. The process of claim 1 , wherein the microporous catalyst component comprises SAPO-34. 10. The process of claim 1 , wherein the metal oxide catalyst component comprises from 1.0 wt % to 99.0 wt % of the hybrid catalyst. 11. The process of claim 1 , wherein the metal oxide catalyst component comprises from 60.0 wt % to 90.0 wt % of the hybrid catalyst. 12. The process of claim 1 , wherein a temperature within the reaction zone during the converting is from 350° C. to 450° C. 13. The process of claim 1 , wherein a pressure within the reaction zone during the converting is at least 1 bar (100 kPa). 14. The process of claim 1 , wherein a GHSV within the reaction zone during the converting is from 1,200/h to 12,000/h. 15. The process of claim 1 , wherein the metal oxide catalyst component is formed by an impregnation method. 16. The process of claim 1 , wherein: the phase pure zirconia comprises crystalline phase pure zirconia; the metal oxide catalyst component comprises from greater than 0.0 g gallium per 100 g phase pure zirconia to 30.0 g gallium per 100 g of phase pure zirconia; and the microporous catalyst component comprises SAPO-34. 17. The process of claim 1 , wherein: a temperature within the reaction zone during the converting is from 350° C. to 450° C.; a pressure within the reaction zone during the converting is at least 1 bar (100 kPa); and a GHSV within the reaction zone during the converting is from 1,200/h to 12,000/h. 18. The process of claim 1 , wherein the phase pure zirconia is a support for the gallium oxide.
of gallium, indium or thallium · CPC title
Mixed oxides other than spinels, e.g. perovskite · CPC title
Silicoaluminophosphates [SAPO compounds] · CPC title
Catalysts containing parts with different compositions · CPC title
less than 10 m2/g · CPC title
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