Methods for making linear internal olefins from mixtures of linear and branched olefins
US-2024051900-A1 · Feb 15, 2024 · US
US12269796B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12269796-B2 |
| Application number | US-202318501076-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 3, 2023 |
| Priority date | Aug 24, 2022 |
| Publication date | Apr 8, 2025 |
| Grant date | Apr 8, 2025 |
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Isomerized olefin products are produced by contacting an olefin feed containing a C 10 to C 20 normal alpha olefin, a solid acid catalyst, and a C 2 to C 15 primary ester to form the isomerized olefin product. Typical primary esters used in the processes include formates and acetates. Linear olefin compositions are produced that contain at least 80 wt. % C 10 to C 20 linear internal olefins, less than 8 wt. % C 10 to C 20 normal alpha olefins, less than 8 wt. % dimers of C 10 to C 20 olefins, less than 15 wt. % C 10 to C 20 branched olefins, and at least 1 wt. % C 2 to C 15 primary ester and less than 8 wt. % secondary esters.
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I claim: 1. A linear internal olefin composition comprising: (a) at least 80 wt. % C 10 to C 20 linear internal olefins; (b) less than or equal to 8 wt. % C 10 to C 20 normal alpha olefin; (c) less than or equal to 8 wt. % dimers of C 10 to C 20 olefins; (d) less than or equal to 15 wt. % C 10 to C 20 branched olefins; and (e) at least 1 wt. % C 2 to C 15 primary ester and less than or equal to 8 wt. % secondary esters. 2. The composition of claim 1 , wherein the composition comprises: (a) at least 85 wt. % C 10 to C 20 linear internal olefins; (b) less than or equal to 3 wt. % C 10 to C 20 normal alpha olefin; and (c) less than or equal to 6 wt. % dimers of C 10 to C 20 olefins. 3. The composition of claim 1 , wherein the composition comprises (e) at least 2 wt. % C 2 to C 15 primary ester and less than or equal to 5 wt. % secondary esters. 4. The composition of claim 1 , wherein the normal alpha olefin has a boiling point that is at least 50° C. greater than that of the primary ester. 5. The composition of claim 1 , wherein the normal alpha olefin has a boiling point that is from 75 to 250° C. greater than that of the primary ester. 6. The composition of claim 1 , wherein the primary ester comprises methyl acetate, ethyl acetate, n-propyl acetate, n-butyl acetate, pentyl acetate, isoamyl acetate, hexyl acetate, heptyl acetate, octyl acetate, nonyl acetate, decyl acetate, methyl formate, ethyl formate, n-propyl formate, n-butyl formate, pentyl formate, isoamyl formate, hexyl formate, heptyl formate, octyl formate, nonyl formate, decyl formate, or any combination thereof. 7. The composition of claim 1 , wherein the primary ester comprises ethyl acetate. 8. The composition of claim 1 , wherein the linear internal olefins comprise a nearly equilibrium distribution of linear double bond isomers. 9. The composition of claim 1 , wherein the composition comprises (a) from 85 to 97 wt. % C 10 to C 20 linear internal olefins. 10. The composition of claim 1 , wherein the composition comprises (b) from 0.1 to 5 wt. % C 10 to C 20 normal alpha olefin. 11. The composition of claim 1 , wherein the composition comprises (c) from 0.1 to 5 wt. % dimers of C 10 to C 20 olefins. 12. The composition of claim 1 , wherein the composition comprises (d) from 0.5 to 7 wt. % C 10 to C 20 branched olefins. 13. The composition of claim 1 , wherein the composition comprises (e) from 1 to 20 wt. % C 2 to C 15 primary ester and from 0.1 to 5 wt. % secondary esters. 14. A linear internal olefin composition comprising: (a) from 80 to 97 wt. % C 10 to C 20 linear internal olefins; (b) from 0.1 to 8 wt. % C 10 to C 20 normal alpha olefin; (c) from 0.1 to 8 wt. % dimers of C 10 to C 20 olefins; (d) from 0.1 to 15 wt. % C 10 to C 20 branched olefins; and (e) from 1 to 15 wt. % C 2 to C 15 primary ester and from 0.1 to 8 wt. % secondary esters. 15. The composition of claim 14 , wherein the normal alpha olefin has a boiling point that is at least 50° C. greater than that of the primary ester. 16. The composition of claim 14 , wherein the normal alpha olefin has a boiling point that is from 75 to 250° C. greater than that of the primary ester. 17. The composition of claim 14 , wherein the primary ester comprises methyl acetate, ethyl acetate, n-propyl acetate, n-butyl acetate, pentyl acetate, isoamyl acetate, hexyl acetate, heptyl acetate, octyl acetate, nonyl acetate, decyl acetate, methyl formate, ethyl formate, n-propyl formate, n-butyl formate, pentyl formate, isoamyl formate, hexyl formate, heptyl formate, octyl formate, nonyl formate, decyl formate, or any combination thereof. 18. The composition of claim 14 , wherein the primary ester comprises ethyl acetate. 19. The composition of claim 14 , wherein the linear internal olefins comprise a nearly equilibrium distribution of linear double bond isomers.
sulfonated · CPC title
Alkenes · CPC title
Isomerisation reactions · CPC title
sulfonated · CPC title
Catalytic processes · CPC title
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