Alcohol mixtures including linear tridecanols
US-2024391857-A1 · Nov 28, 2024 · US
US10450250B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10450250-B2 |
| Application number | US-201615757685-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 16, 2016 |
| Priority date | Sep 17, 2015 |
| Publication date | Oct 22, 2019 |
| Grant date | Oct 22, 2019 |
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The present invention relates to an improved way for the production of farnesol.
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The invention claimed is: 1. A process for the production of the compound of formula (I): wherein the process comprises the steps of: (1) reacting a compound of formula (II): by a rearrangement process in the presence of: (i) at least one mononuclear vanadium catalyst having the following formula: wherein R is an alkyl or aryl group or a M(R 1 ) 3 group, where M is Si, Sn or Ge and R 1 is an alkyl or aryl group, and wherein the catalyst is present in a weight ratio of the compound of formula (II) to the catalyst in a range of 10:1 to 500:1, and (ii) 0.001 to 0.015 mol equivalent relative to the compound of formula (II) at least one least one saturated fatty acid with a 16-22 carbon chain selected from the group consisting of stearic acid, palmitic acid, arachidic acid and behenic acid to thereby form a compound of formula (III): and thereafter (2) conducting hydrogenation of the compound of formula (III) to the compound of formula (I). 2. The process according to claim 1 , wherein the mononuclear vandium catalyst is at least one catalyst compound selected from the group consisting of: 3. The process according to claim 1 , wherein the reaction of step (1) is carried out in at least one non-polar aprotic solvent. 4. The process according to claim 3 , wherein the at least one non-polar aprotic solvent is selected from aliphatic solvents having a boiling point above 280° C., and aromatic solvents. 5. The process according to claim 1 , wherein the reaction of step (1) is carried out at a temperature between 30° C. and 180° C. 6. The process according to claim 1 wherein the hydrogenation of step (2) is carried out with H 2 gas. 7. The process according to claim 1 , wherein the hydrogenation of step (2) is a transfer hydrogenation. 8. The process according to claim 7 , wherein the transfer hydrogenation is carried out in the presence of at least one metal-complex, wherein the metal is selected from the group consisting of Ir, Rh and Ru. 9. The process according to claim 8 , wherein the metal-complex is selected from the group consisting of pentamethylcyclopentadienyl Ir-complex (Cp*Ir), pentamethylcyclopentadienyl Rh-complex (Cp*Rh) and Ru-arene-complexes. 10. The process according to claim 8 , wherein the metal-complex also comprises at least one organic ligand which comprises at least one N and/or P atom. 11. The process according to claim 10 , wherein the at least one organic ligand comprises 1,2 amino alcohols and/or mono-sulfonated 1,2-diamines. 12. The process according to claim 7 , wherein the transfer hydrogenation is carried out in the presence of at least one alcohol or a salt thereof, formic acid or a salt thereof or a formic acid/trimethylamine complex. 13. The process according to claim 4 , wherein the solvent is xylene or toluene. 14. The process according to claim 9 , wherein the metal-complex is a Ru-p-cymene complex or a Ru-benzene complex.
the singly bound functional group being a free hydroxyl group · CPC title
with hydrogen or hydrogen-containing gases · CPC title
of a —CHO group · CPC title
Cyclic compounds, e.g. cyclopentadienyls · CPC title
also containing elements or functional groups covered by B01J31/0201 - B01J31/0269 · CPC title
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