Catalysts comprising a zirconia and gallium oxide component for production of C2 to C4 olefins

US11986799B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11986799-B2
Application numberUS-201917417846-A
CountryUS
Kind codeB2
Filing dateDec 16, 2019
Priority dateDec 28, 2018
Publication dateMay 21, 2024
Grant dateMay 21, 2024

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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Abstract

Official abstract text for this publication.

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.

First claim

Opening claim text (preview).

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.

Assignees

Inventors

Classifications

  • B01J23/08Primary

    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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What does patent US11986799B2 cover?
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…
Who is the assignee on this patent?
Dow Global Technologies Llc, Dow Global Tech Lllc
What technology area does this patent fall under?
Primary CPC classification B01J23/08. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue May 21 2024 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).