Red mud as a catalyst for the isomerization of olefins

US11420915B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11420915-B2
Application numberUS-202016899254-A
CountryUS
Kind codeB2
Filing dateJun 11, 2020
Priority dateJun 11, 2020
Publication dateAug 23, 2022
Grant dateAug 23, 2022

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  1. Title

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  2. Abstract

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  4. Key dates

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  5. First independent claim

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Abstract

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A systems and a method for isomerizing a feedstock to form an alpha-olefin product stream are provided. An exemplary method includes calcining the red mud, flowing an olefin feedstock over the red mud in an isomerization reactor, and separating the alpha-olefin from a reactor effluent.

First claim

Opening claim text (preview).

What is claimed is: 1. A method for isomerization of olefins comprising: calcining a red mud catalyst; isomerizing an olefin feedstock over the calcined red mud catalyst in a reactor to form an effluent; and separating the effluent to obtain an alpha-olefin stream and an alpha-olefin depleted stream. 2. The method of claim 1 , wherein the olefin feedstock comprises 2-butene and the effluent comprises 1-butene. 3. The method of claim 1 , wherein the calcining is conducted to dry the catalyst, remove volatile gases, or both, at a temperature of between about 500° C. and about 800° C. for between about 10 minutes and about 150 minutes. 4. The method of claim 1 , wherein the calcining is conducted to dry the catalyst, remove volatile gases, or both, at a temperature of between about 600° C. and about 700° C. for between about 30 minutes and about 130 minutes. 5. The method of claim 1 , wherein the calcining is conducted to dry the catalyst, remove volatile gases, or both, at a temperature of about 650° C. for about 45 minutes. 6. The method of claim 1 , further comprising activating the calcined catalyst at a temperature of between about 400° C. and about 700° C. for between about 2 hours and about 6 hours. 7. The method of claim 1 , further comprising activating the calcined catalyst at a temperature of between about 500° C. and about 600° C. for between about 3 hours and about 5 hours. 8. The method of claim 1 , further comprising activating the calcined catalyst at a temperature of about 650° C. for about 4 hours. 9. The method of claim 1 , wherein the olefin feedstock is obtained from an upstream purification system in a refinery. 10. The method of claim 1 , wherein the olefin feedstock has a boiling point range of between about −30° C. and about 40° C. and comprises butene. 11. The method of claim 1 , wherein the olefin feedstock has a boiling point range of between about −20° C. and about 10° C. and comprises butene. 12. The method of claim 1 , wherein the olefin feedstock has a boiling point range of between about −10° C. and about 0° C. and comprises butene. 13. The method of claim 1 , further comprising flowing the feedstock over the red mud at a weight hour space velocity of between about 400 hr −1 and 1300 hr −1 . 14. The method of claim 1 , further comprising flowing the feedstock over the red mud at a weight hour space velocity of between about 650 hr −1 and 1150 hr −1 . 15. The method of claim 1 , further comprising flowing the feedstock over the red mud at a weight hour space velocity of about 900 hr −1 . 16. The method of claim 1 , wherein the separating is performed in a distillation column. 17. The method of claim 1 , wherein the alpha-olefin stream comprises 1-butene and the separating is performed in a distillation column. 18. The method of claim 1 , further comprising passing the alpha-olefin depleted stream to an upstream purification system. 19. The method of claim 1 , further comprising combining the alpha-olefin depleted stream with the olefin feedstock.

Assignees

Inventors

Classifications

  • with alkali- or alkaline earth metals · CPC title

  • Decomposition of a metal salt · CPC title

  • with metal oxides · CPC title

  • B01J37/08Primary

    Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

  • Chemical, physical or physico-chemical processes in general; Their relevant apparatus · CPC title

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What does patent US11420915B2 cover?
A systems and a method for isomerizing a feedstock to form an alpha-olefin product stream are provided. An exemplary method includes calcining the red mud, flowing an olefin feedstock over the red mud in an isomerization reactor, and separating the alpha-olefin from a reactor effluent.
Who is the assignee on this patent?
Saudi Arabian Oil Co
What technology area does this patent fall under?
Primary CPC classification B01J37/08. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Aug 23 2022 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 12 related publications on this page (citations in our corpus or others sharing the same primary CPC).