Stabilized rhenium-based heterogeneous catalyst and use thereof

US10143997B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10143997-B2
Application numberUS-201515524026-A
CountryUS
Kind codeB2
Filing dateAug 4, 2015
Priority dateAug 5, 2014
Publication dateDec 4, 2018
Grant dateDec 4, 2018

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

The present invention relates to a stabilized rhenium-based heterogeneous catalyst, obtainable by a process comprising contacting a rhenium-based heterogeneous catalyst with a stabilizing agent at a temperature in a range from 0-100° C., the stabilizing agent comprising an aliphatic hydrocarbon compound and use thereof.

First claim

Opening claim text (preview).

The invention claimed is: 1. A process for preparing an olefin hydrocarbon compound, the process comprising: contacting, in the absence of an olefin feed stream, a rhenium-based heterogeneous catalyst with a stabilizing agent comprising an aliphatic hydrocarbon selected from the group consisting of ethane, ethylene, propane, and propylene, to provide a stabilized rhenium-based heterogeneous catalyst, followed by reacting the olefin feed stream in the presence of the stabilized rhenium-based heterogeneous catalyst to obtain the olefin hydrocarbon compound, wherein the olefin feed stream comprises a C4 olefin, a C5 olefin, or a mixture thereof, and wherein the reacting is carried out at a temperature in a range from 0 to 300° C. 2. The process according to claim 1 , wherein the contacting is carried out at a temperature from 0° C. to 100° C. to provide the stabilized rhenium-based heterogeneous catalyst. 3. The process according to claim 1 , wherein the contacting is carried out at a temperature from 10° C. to 60° C. to provide the stabilized rhenium-based heterogeneous catalyst. 4. The process according to claim 1 , wherein the reacting of the olefin feed stream in the presence of the stabilized rhenium-based heterogeneous catalyst is carried out in a fixed bed reactor. 5. The process of claim 1 , wherein the olefin feed stream comprises (i) ethylene and a C4 linear olefin, (ii) ethylene and a C5 linear olefin, or (iii) ethylene and both C4 and C5 linear olefins. 6. The process according to claim 3 , wherein the contacting is carried out at a temperature from 20 to 40° C. 7. The process of claim 1 , wherein the rhenium-based heterogeneous catalyst comprises elemental rhenium or a rhenium compound, wherein rhenium is present in an amount from 0.01% to 20% by weight of the catalyst. 8. The process of claim 1 , wherein the rhenium-based heterogeneous catalyst comprises elemental rhenium or a rhenium compound, disposed on a solid support comprising Al 2 O 3 , Ga 2 O 3 , SiO 2 , GeO 2 , TiO 2 , ZrO 2 , SnO 2 , aluminosilicate, activated carbon, hydrotalcite, an anionic clay, or a mixture thereof. 9. The process of claim 8 , wherein the solid support comprises Al 2 O 3 or SiO 2 . 10. The process of claim 8 , wherein the rhenium-based heterogeneous catalyst comprises elemental rhenium, rhenium oxide, rhenium hydride, rhenium sulfide, or rhenium carbide. 11. The process of claim 1 , wherein the contacting provides the stabilized rhenium-based heterogeneous catalyst with increased conversion stability and/or increased selectivity to the olefin hydrocarbon compound, relative to performing the reacting alone. 12. The process of claim 11 , wherein the olefin feed stream comprises oxygenated compounds. 13. The process of claim 1 , wherein the olefin hydrocarbon compound is propylene that is obtained from an olefin metathesis reaction, with ethylene, of the C4 olefin and/or the C5 olefin of the olefin feed stream. 14. The process of claim 1 , wherein the rhenium-based heterogeneous catalyst has been subjected to regeneration, prior to the contacting. 15. A process for preparing an olefin hydrocarbon compound, the process comprising: contacting, in the absence of an olefin feed stream, a rhenium-based heterogeneous catalyst with a flow of a stabilizing gas comprising an aliphatic hydrocarbon compound selected from the group consisting of ethane, ethylene, propane, and propylene, to provide a stabilized rhenium-based heterogeneous catalyst, followed by reacting the olefin feed stream in the presence of the stabilized rhenium-based heterogeneous catalyst to obtain the olefin hydrocarbon compound, wherein the olefin feed stream comprises at least one olefin selected from the group consisting of C4 to C12 olefins, and wherein the reacting is carried out at a temperature in a range from 0 to 300° C. 16. The process of claim 15 , wherein the olefin feed stream comprises (i) a C2 olefin and a C4 olefin or (ii) a C2 olefin and a C5 olefin. 17. The process of claim 15 , wherein the olefin feed stream comprises oxygenated compounds. 18. A process for preparing an olefin hydrocarbon compound, the process comprising: contacting a rhenium-based heterogeneous catalyst with a stabilizing agent comprising ethane or propane, to provide a stabilized rhenium-based heterogeneous catalyst, followed by reacting an olefin feed stream in the presence of the stabilized rhenium-based heterogeneous catalyst to obtain the olefin hydrocarbon compound, wherein the olefin feed stream comprises at least one olefin selected from the group consisting of C2 to C12 olefins, and wherein the reacting is carried out at a temperature in a range from 0 to 300° C. 19. The process of claim 18 , wherein the contacting provides the stabilized rhenium-based heterogeneous catalyst with increased conversion stability and/or increased selectivity to the olefin hydrocarbon compound, relative to performing the reacting alone. 20. The process of claim 18 , wherein the rhenium-based heterogeneous catalyst has been subjected to regeneration, prior to the contacting.

Assignees

Inventors

Classifications

  • using catalysts, e.g. selective catalysts · CPC title

  • of gallium, indium or thallium · CPC title

  • Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof · CPC title

  • Rhenium · CPC title

  • Metathesis reactions, e.g. olefin metathesis · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US10143997B2 cover?
The present invention relates to a stabilized rhenium-based heterogeneous catalyst, obtainable by a process comprising contacting a rhenium-based heterogeneous catalyst with a stabilizing agent at a temperature in a range from 0-100° C., the stabilizing agent comprising an aliphatic hydrocarbon compound and use thereof.
Who is the assignee on this patent?
Scg Chemicals Co Ltd
What technology area does this patent fall under?
Primary CPC classification B01J23/36. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Dec 04 2018 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 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).