Hybrid catalyst for selective and stable olefin production

US11548835B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11548835-B2
Application numberUS-201816757694-A
CountryUS
Kind codeB2
Filing dateOct 11, 2018
Priority dateOct 30, 2017
Publication dateJan 10, 2023
Grant dateJan 10, 2023

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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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  7. Citations and related patents

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Abstract

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A process for preparing C2 to C5 olefins includes introducing a feed stream comprising hydrogen and at least one carbon-containing component selected from the group consisting of CO, CO2, and mixtures thereof into a reaction zone. The feed stream is contacted with a hybrid catalyst in the reaction zone, and a product stream is formed that exits the reaction zone and includes C2 to C5 olefins. The hybrid catalyst includes a methanol synthesis component and a solid microporous acid component that is selected from molecular sieves having 8-MR access and having a framework type selected from the group consisting of CHA, AEI, AFX, ERI, LTA, UFI, RTH, and combinations thereof. The methanol synthesis component comprises a metal oxide support and a metal catalyst. The metal oxide support includes titania, zirconia, hafnia or mixtures thereof, and the metal catalyst includes zinc.

First claim

Opening claim text (preview).

The invention claimed is: 1. A process for preparing C 2 to C 5 olefins, comprising: introducing a feed stream comprising hydrogen and at least one carbon-containing component selected from the group consisting of CO, CO 2 , and mixtures thereof into a reaction zone; contacting the feed stream with a hybrid catalyst in the reaction zone to synthesize C2 to C5 olefins, wherein the hybrid catalyst comprises a methanol synthesis component and a solid microporous acid component that is selected from molecular sieves having 8-MR access and having a framework type selected from the group consisting of the following framework types CHA, AEI, AFX, ERI, LTA, UFI, RTH, and combinations thereof, the framework types corresponding to the naming convention of the International Zeolite Association, wherein the methanol synthesis component comprises a metal oxide support and a metal catalyst, wherein the metal oxide support comprises titania, zirconia, hafnia or mixtures thereof, and the metal catalyst comprises zinc; and forming a product stream that exits the reaction zone, wherein the product stream comprises C 2 to C 5 olefins. 2. The process according to claim 1 , wherein a surface area of the metal oxide support is greater than or equal to 20 m 2 /g. 3. The process according to claim 1 , wherein the metal oxide support comprises titania or a mixture of titania and zirconia. 4. The process according to claim 1 , wherein the solid microporous acid component is SAPO-34. 5. The process according to claim 1 , wherein the metal catalyst further comprises copper, chromium, manganese, and mixtures thereof. 6. The process according to claim 1 , wherein a loading of the metal catalyst, measured per 100 mg of metal oxide support, is from greater than or equal to 0.8 mg of metal catalyst/100 mg of metal oxide support to less than or equal to 50.0 mg of metal catalyst/100 mg of metal oxide support. 7. The process according to claim 1 , wherein the metal oxide support comprises titania and an atomic ratio (at/at) of zinc to titania (Zn/Ti) is from greater than or equal to 0.01 to less than or equal to 0.61, or the metal oxide support comprises zirconia and an atomic ratio (at/at) of zinc to zirconia (Zn/Zr) is from greater than or equal to 0.01 to less than or equal to 0.94. 8. The process according to claim 1 , wherein the methanol synthesis component is calcined at a temperature less than 800° C. 9. The process according to claim 1 , wherein a carbon monoxide conversion is greater than or equal to 15%. 10. The process according to claim 1 , wherein a carbon yield of C 2 to C 5 olefins is greater than or equal to 3.6%. 11. The process according to claim 1 , wherein an integral productivity of the hybrid catalyst is greater than or equal to 2.5 kg olefins/liter (l) of catalyst in 1000 h time.

Assignees

Inventors

Classifications

  • containing iron group metals, noble metals or copper · CPC title

  • containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead · CPC title

  • C07C1/043Primary

    characterised by the composition · CPC title

  • Feedstock · CPC title

  • A-type · CPC title

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What does patent US11548835B2 cover?
A process for preparing C2 to C5 olefins includes introducing a feed stream comprising hydrogen and at least one carbon-containing component selected from the group consisting of CO, CO2, and mixtures thereof into a reaction zone. The feed stream is contacted with a hybrid catalyst in the reaction zone, and a product stream is formed that exits the reaction zone and includes C2 to C5 olefins. T…
Who is the assignee on this patent?
Dow Global Technologies Llc, Dow Global Tech
What technology area does this patent fall under?
Primary CPC classification C07C1/043. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Jan 10 2023 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 3 related publications on this page (citations in our corpus or others sharing the same primary CPC).