Production method of 2,7-octadien-1-ol
US-2025188007-A1 · Jun 12, 2025 · US
US9315433B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9315433-B2 |
| Application number | US-201414778798-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 26, 2014 |
| Priority date | Mar 27, 2013 |
| Publication date | Apr 19, 2016 |
| Grant date | Apr 19, 2016 |
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Provided is a simple and industrially advantageous method for producing 2,7-octadien-1-ol, in which an expensive palladium catalyst is recovered in high efficiency and the reaction rate per atom of palladium is enhanced. Specifically, provided is a method for producing 2,7-octadien-1-ol by subjecting butadiene and water to a telomerization in the presence of a palladium catalyst containing a water-soluble triarylphosphine having two or more sulfonate groups in the molecule and a palladium compound, a tertiary amine, and carbon dioxide, including a step of mixing the telomerization solution obtained by the telomerization with an organic solvent having a dielectric constant at 25° C. of 2 to 18, followed by carrying out phase separation in the presence of carbon dioxide, thereby obtaining 2,7-octadien-1-ol from an organic phase while recovering an aqueous phase including the palladium catalyst. By this production method, the selectivity for 2,7-octadien-1-ol is enhanced.
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The invention claimed is: 1. A method for producing 2,7-octadien-1-ol, comprising: subjecting butadiene and water to a telomerization in the presence of a palladium catalyst, a tertiary amine and carbon dioxide, the palladium catalyst comprising a water-soluble triarylphosphine and a palladium compound, the water-soluble triarylphosphine comprising two or more sulfonate groups; mixing a telomerization solution obtained by the telomerization with an organic solvent having a dielectric constant of 2 to 18 at 25° C. to form a liquid having an aqueous phase and an organic phase; and carrying out phase separation of the liquid in the presence of carbon dioxide by recovering the 2,7-octadien-1-ol from the organic phase while retaining the palladium catalyst in the aqueous phase. 2. The method of according to claim 1 , wherein the water-soluble triarylphosphine is represented by the following general formula (I): wherein: R 1 , R 2 , R 3 , R 4 , R 5 , and R 6 each independently represent a hydrogen atom, an alkyl group having 1 to 4 carbon atoms, or an alkoxy group having 1 to 4 carbon atoms; R 7 , R 8 , and R 9 each independently represent an alkyl group having 1 to 4 carbon atoms or an alkoxy group having 1 to 4 carbon atoms; p, q, and r each independently represent an integer of 0 to 2; M's may be the same as or different from each other, and each M represents a cation of a metal atom belonging to Group 1 or an ammonium cation derived from a tertiary amine where the total number of carbon atoms of a group bonded to the nitrogen atom of the tertiary amine is 3 to 27; n represents 0 or 1; and sulfonate groups (—SO 3 M) are each at a meta-binding position or a para-binding position to the phosphorous atom of the water-soluble triarylphosphine. 3. The method according to claim 2 , wherein: R 1 , R 3 , R 5 , R 7 , R 8 , and R 9 each independently represent a hydrogen atom, a methyl group, or a methoxy group; R 2 , R 4 , and R 6 are a hydrogen atom; M's each independently represent a cation of an alkali metal atom or the ammonium cation derived from a tertiary amine; and the sulfonate groups (—SO 3 M) are each at the meta-binding position to the phosphorous atom of the water-soluble triarylphosphine. 4. The method according to claim 2 , wherein: R 1 , R 2 , R 3 , R 4 , R 5 , and R 6 each independently represent a hydrogen atom, a methyl group, or a methoxy group; p, q, and r are each 0; M's each independently represent a cation of a lithium atom, a cation of a sodium atom, a cation of a potassium atom, or the ammonium cation derived from a tertiary amine; and the sulfonate groups (—SO 3 M) are each at a diagonal binding position of R 1 , R 3 , or R 5 on the benzene ring. 5. The method according to claim 4 , wherein: R 1 , R 3 , and R 5 are all the same as each other and each represent a hydrogen atom or a methyl group; p, q, and r are each 0, and M's are the same as each other and each represent a cation of a lithium atom, a cation of a sodium atom, a cation of a potassium atom, or the ammonium cation derived from a tertiary amine. 6. The method according to claim 2 , wherein: at least two of R 1 , R 3 , and R 5 are each an alkyl group having 1 to 4 carbon atoms or an alkoxy group having 1 to 4 carbon atoms. 7. The method according to claim 6 , wherein at least two of R 1 , R 3 , and R 5 are each a methyl group. 8. The method according to claim 2 , wherein M is an ammonium cation derived from a tertiary amine where the total number of carbon atoms of a group bonded to the nitrogen atom of the tertiary amine is 5 to 24. 9. The method according to claim 8 , wherein M is an ammonium cation derived from a tertiary amine wherein the total number of carbon atoms of a group bonded to the nitrogen atom of the tertiary amine is 5 to 7. 10. The method according to claim 1 , wherein the phase separation is carried out at a temperature of 130° C. or lower and a total pressure, after introduction of carbon dioxide, of 0.1 MPa (gauge pressure) or more. 11. The method according to claim 10 , wherein the phase separation is carried out at a temperature of 5° C. to 90° C., and a total pressure, after introduction of carbon dioxide, of 0.5 MPa to 3 MPa (gauge pressure). 12. The method according to claim 1 , wherein the telomerization is carried out at a temperature of 130° C. or lower and a total pressure, after introduction of carbon dioxide, of 0.5 MPa (gauge pressure) or more. 13. The method according to claim 1 , wherein at least a part of the palladium catalyst in the aqueous phase is reused in the telomerization.
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