Systems and methods of privacy within a security system
US-2018197400-A1 · Jul 12, 2018 · US
US11801499B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11801499-B2 |
| Application number | US-202117359360-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 25, 2021 |
| Priority date | Dec 26, 2018 |
| Publication date | Oct 31, 2023 |
| Grant date | Oct 31, 2023 |
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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.
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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.
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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