Process for the chemoselective reduction of terminally saturated carboxylic esters
US-9193651-B2 · Nov 24, 2015 · US
US9701615B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9701615-B2 |
| Application number | US-201415035447-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 6, 2014 |
| Priority date | Nov 8, 2013 |
| Publication date | Jul 11, 2017 |
| Grant date | Jul 11, 2017 |
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A method for synthesising a second ester from a first ester, the method including the following steps: a) placing a first ester and a catalyst in the presence of dihydrogen such as to obtain a first alcohol and a second alcohol; b) extracting the second alcohol from the reaction medium; c) reacting the first alcohol with the catalyst of step a) in order to obtain a second ester and dihydrogen; and d) recirculating the dihydrogen obtained in step c) by injecting same into step a).
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The invention claimed is: 1. A method for synthesizing a second ester from a first ester which comprises the following steps: a) bringing a first ester and a catalyst of formula 1 and dihydrogen into contact in order to obtain a first alcohol and a second alcohol; b) separating said second alcohol from the reaction medium; c) reacting said first alcohol with the catalyst of formula 1 from step a) in order to obtain a second ester and dihydrogen; and d) recycling the dihydrogen obtained in step c) by introducing it into step a); said formula 1 being: where R are groups, which may be identical or different, selected from the group consisting of cyclohexyl, phenyl, isopropyl and ethyl; where Y is a PR′ 3 phosphine, a CO radical or a hydrogen atom, R′, which are identical or different, being C 1 -C 12 alkyl groups or C 6 -C 12 aryl groups; and where Z is a hydrogen atom, a HBH 3 group or a halogen atom. 2. The method as claimed in claim 1 , wherein step c) of the method is carried out without addition of a hydrogen acceptor. 3. The method as claimed in claim 1 , wherein the step(s) a) and/or c) of the method is/are carried out without addition of solvent. 4. The method as claimed in claim 3 , wherein the step(s) a) and/or c) of the method is/are carried out without addition of base. 5. The method as claimed in claim 1 , wherein Z is not a halogen atom. 6. The method as claimed in claim 1 , wherein the R′ group is a methyl, ethyl, isopropyl or phenyl group. 7. The method as claimed in claim 1 , wherein R is a cyclohexyl or isopropyl group. 8. The method as claimed in claim 1 , wherein said first ester has the following formula: where R 1 is a C 2 to C 32 alkyl group, and R 2 is a C 1 to C 6 alkyl group. 9. The method as claimed in claim 1 , wherein said first ester has the following formula: where R 3 are identical or different C 2 to C 32 alkyl groups. 10. The method as claimed in claim 1 , wherein the loading of said catalyst of formula 1 used in step b) is selected from a range extending from 500 ppm to 1 ppm. 11. The method as claimed in claim 1 , wherein step a) is carried out under reaction conditions comprising: i) a temperature ranging from 5° C. to 150° C. ii) a pressure of dihydrogen ranging from 1 bar to 50 bar. 12. The method as claimed in claim 1 , wherein step c) is carried out under reaction conditions comprising: i) a temperature ranging from 5° C. to 200° C.; ii) a pressure that allows the concomitant release of hydrogen. 13. The method as claimed in claim 12 , wherein said pressure that allows the release of hydrogen is a pressure equal to or below atmospheric pressure. 14. A method of catalytic synthesis, comprising the use of a catalyst of formula 1: where R are groups, which may be identical or different, selected from the group consisting of cyclohexyl, phenyl, isopropyl and ethyl; where Y is a PR′ 3 phosphine, a CO radical or a hydrogen atom, R′, which are identical or different, being C 1 -C 12 alkyl groups or C 6 -C 12 aryl groups; and where Z is a hydrogen atom, a HBH 3 group or a halogen atom, in order to carry out a catalytic synthesis, said synthesis comprising the following steps: a) bringing a first ester and a catalyst of formula 1 and dihydrogen into contact in order to obtain a first alcohol and a second alcohol; b) separating said second alcohol from the reaction medium. 15. The method as claimed in claim 14 , wherein said first ester is a fatty acid methyl ester. 16. The method as claimed in claim 11 , wherein step a) is carried out under reaction conditions comprising: i) a temperature ranging from 75° C. to 125° C.; ii) a pressure of dihydrogen ranging from 1 bar to 50 bar. 17. The method as claimed in claim 11 , wherein step a) is carried out under reaction conditions comprising: i) a temperature ranging from 5° C. to 150° C.; and ii) a pressure of dihydrogen ranging 10 to 30 bar. 18. The method as claimed in claim 11 , wherein step a) is carried out under reaction conditions comprising: i) a temperature ranging from 75° C. to 125° C.; and ii) a pressure of dihydrogen ranging 10 to 30 bar. 19. The method as claimed in claim 10 , wherein the loading of said catalyst of formula 1 used in step b) is selected from a range extending from 200 ppm to 20 ppm. 20. The method as claimed in claim 12 , wherein step c) is carried out under reaction conditions comprising: i) a temperature ranging from 100° C. to 150° C.; ii) a pressure that allows the concomitant release of hydrogen.
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Preparation of carboxylic acid esters · CPC title
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