Catalyst for producing light olefins from C4-C7 hydrocarbons

US11801499B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11801499-B2
Application numberUS-202117359360-A
CountryUS
Kind codeB2
Filing dateJun 25, 2021
Priority dateDec 26, 2018
Publication dateOct 31, 2023
Grant dateOct 31, 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

Official abstract text for this publication.

The present invention relates to a catalyst for producing light olefins from C4-C7 hydrocarbons from catalytic cracking reaction and the production process of light olefins from said catalyst, wherein said catalyst has core-shell structure comprising a zeolite core with mole ratio of silicon to aluminium (Si/Al) between 2 to 250 and layered double hydroxide shell (LDH). The catalyst according to the invention provides high percent conversion of substrate to products and high selectivity to light olefins product.

First claim

Opening claim text (preview).

The invention claimed is: 1. A catalyst for producing light olefins from C4-C7 hydrocarbons, wherein said catalyst has a core-shell structure comprising a zeolite core with mole ratio of silicon to aluminium (Si/Al) between 2 to 250 and a layered double hydroxide shell and said zeolite is a hierarchical zeolite. 2. The catalyst according to claim 1 , wherein said zeolite is the hierarchical zeolite comprising a micropore with size between 0.3 to 0.6 nm, a mesopore with size between 2 to 10 nm, and a macropore with size larger than 50 nm, wherein the mesopore and macropore proportions are greater than or equal to 15 to 60% when compared to a total pore volume. 3. The catalyst according to claim 1 , wherein said zeolite has the mole ratio of silicon to aluminium between 15 to 30. 4. The catalyst according to claim 3 , wherein said zeolite has the mole ratio of silicon to aluminium of equal to 15. 5. The catalyst according to claim 1 , wherein said zeolite is selected from zeolite types ZSM-5, FAU, MOR, BETA or FER. 6. The catalyst according to claim 1 , wherein said zeolite has a crystal size between 100 to 3,000 nm. 7. The catalyst according to claim 1 , wherein the primary metals presented in said layered double hydroxide are the group 2 metals and the group 3 metals. 8. The catalyst according to claim 7 , wherein the primary metals presented in said layered double hydroxide are magnesium (Mg) and aluminium (Al). 9. The catalyst according to claim 1 , wherein said layered double hydroxide has a mole ratio of magnesium to aluminium between 1 to 3. 10. The catalyst according to claim 9 , wherein said layered double hydroxide has the mole ratio of magnesium to aluminium between 1 to 2. 11. The catalyst according to claim 1 , wherein said layered double hydroxide has a thickness between 100 to 1,000 nm. 12. The catalyst according to claim 1 , wherein the catalyst comprises a core and a shell which has a mass ratio of shell:core between 1:1 to 1:7. 13. The catalyst according to claim 1 , wherein the catalyst comprises a core and a shell which has a mass ratio of shell:core between 1:2 to 1:6. 14. A production process of light olefins from catalytic cracking reaction of C4-C7 hydrocarbons comprising: contacting C4-C7 hydrocarbons with a catalyst, wherein said catalyst has a core-shell structure comprising a zeolite core with mole ratio of silicon to aluminium (Si/Al) between 2 to 250 and a layered double hydroxide shell and said zeolite is a hierarchical zeolite. 15. The process according to claim 14 , wherein said process is operated at temperature between 450 to 650° C. and pressure between atmospheric pressure 1 to 5 bars. 16. The process according to claim 14 or 15 , wherein the C4-C7 hydrocarbons are selected from butane, pentane, hexane, or heptane. 17. The process according to claim 16 , wherein the C4-C7 hydrocarbons are pentane. 18. The process according to claim 14 , wherein the light olefins are ethylene and propylene.

Assignees

Inventors

Classifications

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

  • of the mordenite type · CPC title

  • having base-exchange properties, e.g. crystalline zeolites, pillared clays · CPC title

  • of the faujasite type, e.g. type X or Y · CPC title

  • of the ferrierite type, e.g. types ZSM-21, ZSM-35 or ZSM-38 · CPC title

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What does patent US11801499B2 cover?
The present invention relates to a catalyst for producing light olefins from C4-C7 hydrocarbons from catalytic cracking reaction and the production process of light olefins from said catalyst, wherein said catalyst has core-shell structure comprising a zeolite core with mole ratio of silicon to aluminium (Si/Al) between 2 to 250 and layered double hydroxide shell (LDH). The catalyst according t…
Who is the assignee on this patent?
Ptt Global Chemical Public Co Ltd
What technology area does this patent fall under?
Primary CPC classification B01J29/40. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Oct 31 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 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).