Gas Phase Production of Alkyl Alkanoate
US-2016229788-A1 · Aug 11, 2016 · US
US9850194B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9850194-B2 |
| Application number | US-201615378514-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 14, 2016 |
| Priority date | Dec 16, 2015 |
| Publication date | Dec 26, 2017 |
| Grant date | Dec 26, 2017 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The invention relates to a process for doubly carbonylating allyl alcohols to the corresponding diesters, wherein a linear or branched allyl alcohol is reacted with a linear or branched alkanol (alcohol) with supply of CO and in the presence of a catalytic system composed of a palladium complex and at least one organic phosphorus ligand and in the presence of a hydrogen halide selected from HCl, HBr and HI.
Opening claim text (preview).
The invention claimed is: 1. Process for doubly carbonylating allyl alcohols to diesters, comprising: reacting, in a single step, a linear or branched allyl alcohol with a linear or branched alkanol with supply of CO and in the presence of a catalytic system composed of a palladium complex and at least one organic phosphorus ligand and in the presence of a hydrogen halide selected from HCl, HBr and HI, wherein both the allyl portion and the alcohol portion of the allyl alcohol are reacted with the CO. 2. Process according to claim 1 , characterized in that the allyl alcohols are compounds of the general formula (1): where R 1 , R 2 and R 3 are independently hydrogen or a C 1 to C 10 alkyl radical and R′ is hydrogen, or a saturated branched or unbranched, aliphatic, cycloaliphatic or cycloaliphatic-aliphatic hydrocarbyl radical having up to 12 carbon atoms, in which C—C bonds may be interrupted by oxygen or the —O—CO— group, or a phenyl radical, where the phenyl radical may be substituted as follows: C 1 - to C 10 -alkyl- or C 1 - to C 10 -alkoxy groups. 3. Process according to claim 1 , characterized in that the alkanols are compounds of the general formula ROH where R is a C 1 - to C 20 -alkyl, a C 1 to C 20 -cycloalkyl or a C 7 - to C 11 -aralkyl group. 4. Process according to claim 1 , characterized in that the reaction is conducted in the liquid phase at a temperature of 70 to 250° C. 5. Process according to claim 1 , characterized in that reaction is conducted under a pressure of 2 to 100 bar. 6. Process according to claim 1 , characterized in that the palladium complex is formed in situ proceeding from a pre-complex, using, as palladium source, palladium-containing salts and complexes as precursor. 7. Process according to claim 6 , characterized in that the palladium complex is selected from the group comprising Pd acetate, Pd acetylacetonate, Pd halides, Pd-halogen-1,5-cyclooctadienes, Pd nitrates, Pd oxide and diammonium hexachloropalladate. 8. Process according to claim 1 , characterized in that the phosphine ligands have a mono- or bidentate structure, preferably selected from the group comprising L1—(9,9-dimethyl-9H-xanthene-4,5-diyl)bis(diphenylphosphine), L2—10,10′-(oxybis(2,1-phenylene))bis(10H-phenoxaphosphinine), L3—2,2′-((9,9-dimethyl-9H-xanthene-4,5-diyl)bis(tert-butylphosphinediyl))dipyridine, L4—(oxybis(2,1-phenylene))bis(tert-butyl(phenyl)phosphine), L5—4,6-bis(diphenylphosphinyl)-10H-phenoxazine, L6—1,3-bis((diphenylphosphinyl)methyl)benzene, L7—(oxybis(2,1-phenylene))bis(di-tert-butylphosphine), L8—(oxybis(2,1-phenylene))bis(di-o-tolylphosphine), L9—bis(2-(diphenylphosphinyl)-5-methylphenyl)methane, L10—1,2-bis((di-tert-butylphosphinyl)methyl)benzene, L11—di(1-adamantyl)-n-butylphosphine, L12—1-(2-(diphenylphosphinyl)benzyl)-1H-pyrrole. 9. Process according to claim 1 , characterized in that the hydrogen halide used is hydrogen chloride. 10. Process according to claim 1 , characterized in that the ratio of palladium to hydrogen halide is in the range from 1:3 to 1:30. 11. Process according to claim 1 , characterized in that a metal halide is added to the reaction, where the ratio of halide to hydrogen halide is in the range from 1:1 to 5:1.
by addition to an unsaturated carbon-to-carbon bond · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.