High density turbine and diesel fuels from tricyclic sesquiterpenes
US-9777234-B1 · Oct 3, 2017 · US
US12152003B1 · US · B1
| Field | Value |
|---|---|
| Publication number | US-12152003-B1 |
| Application number | US-202318128520-A |
| Country | US |
| Kind code | B1 |
| Filing date | Mar 30, 2023 |
| Priority date | Mar 31, 2022 |
| Publication date | Nov 26, 2024 |
| Grant date | Nov 26, 2024 |
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The present invention provides a novel method for chemoselectively hydrogenating cyclic monoterpene precursors with reduced PtO 2 at low temperatures, to yield products in which the alkene groups are saturated while the cyclopropane rings from the parent hydrocarbons are conserved.
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The invention claimed is: 1. A method for the chemoselective hydrogenation of cycloalkene, comprising obtaining a cycloalkene having at least one alkene group and at least one cyclopropane group; and, hydrogenating the cycloalkene with a catalyst; controlling the degree of hydrogenation through temperature; wherein the at least one alkene group is saturated and the at least one cyclopropane group is conserved. 2. The method of claim 1 , further comprising purifying the hydrogenated cycloalkene by filtration, washing, and distillation. 3. The method of claim 1 , wherein the cycloalkene is a monoterpene (C10), a sesquiterpene (C15), a diterpene (C20), a heavier oligomer, or combinations thereof. 4. The method of claim 3 , wherein the cycloalkene is sabinene, thujene, 3-carene, 2-carene, thujopsene, or combinations thereof. 5. The method of claim 1 wherein controlling the degree of hydrogenation further comprises catalyst selection. 6. The method of claim 5 , wherein the catalyst is a heterogenous catalyst. 7. The method of claim 5 , wherein the catalyst is a platinum-based hydrogenation catalyst. 8. The method of claim 5 , wherein the catalyst is a Pd-based hydrogenation catalyst. 9. The method of claim 5 , wherein the catalyst is about 0.0001 to about 1 mol %. 10. The method of claim 1 , wherein the hydrogenation is conducted at or below ambient temperature. 11. The method of claim 1 , wherein the hydrogenation is conducted at between about −80° C. to about 50° C. 12. The method of claim 1 , wherein the hydrogenation is conducted at low pressure between about 1 to about 100 psi. 13. The method of claim 1 wherein a carboxylic acid is added as a co-solvent. 14. The method of claim 13 wherein the carboxylic acid as added in about a 1:5 to about a 1:10 ratio of carboxylic acid:cycloalkane. 15. The method of claim 13 wherein the carboxylic acid is acetic acid. 16. A fuel blend comprising jet fuel and the hydrogenated cycloalkene produced by the method of claim 1 .
Platinum · CPC title
with a ring being at least seven-membered · CPC title
the ring being saturated · CPC title
with simultaneous isomerisation · CPC title
the ring system containing six carbon atoms · CPC title
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