Process for separating hydrocarbon compounds
US-2015368167-A1 · Dec 24, 2015 · US
US10040732B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10040732-B2 |
| Application number | US-201515326860-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 15, 2015 |
| Priority date | Jul 17, 2014 |
| Publication date | Aug 7, 2018 |
| Grant date | Aug 7, 2018 |
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Process for producing biaryl compounds by aerobic cross dehydrogenative coupling (CDC) of two arene groups comprising at least one aryl carbon-hydrogen bond, in the presence of a catalyst system comprising a palladium salt comprising at least one non-cyclopalladatable carboxylate anion and one or more non-beta-eliminatable, non-cyclopalladatable ligands comprising at least one N-donor atom, the one or more ligands having a 0.5/1-1.5/1 molar ratio of N-donor atoms relative to the Pd atoms.
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The invention claimed is: 1. Process for producing biaryl compounds by aerobic cross dehydrogenative coupling (CDC) of two arene groups comprising at least one aryl carbon-hydrogen bond, in the presence of a catalyst system comprising a palladium salt comprising at least one non-cyclopalladatable carboxylate anion and one or more non-beta-eliminatable, non-cyclopalladatable ligands comprising at least one N-donor atom, the one or more ligands having a 0.5/1-1.5/1 molar ratio of N-donor atoms relative to the Pd atoms. 2. Process according to claim 1 , wherein the molar ratio of N-donor atoms relative to the Pd atoms is between 0.7/1 and 1.3/1. 3. Process according to claim 1 , wherein the molar ratio of N-donor atoms relative to the Pd atoms is between 0.8/1 and 1.2/1. 4. Process according to claim 1 , wherein aliphatic cyclic or non-cyclic primary, secondary or tertiary amines, aromatic N-heterocycles and/or benzofused derivatives thereof are used as the one or more ligands. 5. Process according to claim 4 , wherein pyridines, pyridazines, pyrimidines, pyrazines, triazines, imidazoles, triazoles, oxazoles, 4,5-dihydrooxazoles, isoxazoles, 4,5-dihydroisoxazoles, and 5,6-dihydro-4H-1,3-oxazines or quinolines, isoquinolines, cinnolines, phthalazines, quinazoline, quinoxalines, 1H-benzo[d]imidazoles, 1H-benzo[d][1,2,3]triazoles, benzo[d]oxazoles, benzo[d]isoxazoles and 4H-benzo[e][1,3]oxazines and/or benzofused derivatives thereof are used as the one or more ligands. 6. Process according to claim 4 , wherein pyridines, pyridazines, pyrimidines, pyrazines, triazines, quinolines, isoquinolines, cinnolines, phthalazine, quinazoline, and quinoxalines and/or benzofused derivatives thereof are used as the one or more ligands. 7. Process according to claim 1 , wherein the process is carried out under a (partial) pressure of oxygen of 0.2-2 bar, and wherein a catalyst system is used comprising a palladium salt comprising at least one non-cyclopalladatable carboxylate anion derived from a carboxylic acid that is triply substituted at the alpha-carbon atom relative to the carboxylate group, with the carboxylic acid also containing at least one beta-carbon atom. 8. Process according to claim 7 , wherein the carboxylate anion is derived from a 2,2-dialkylalkanoic acid, 2-fluoro-2-alkylalkanoic acid, 2,2-difluoroalkanoic acid, 2,2-difluoro-2-arylacetic acid, with the alkanoic acid containing at least one beta-carbon atom. 9. Process according to claim 7 , wherein the carboxylate anion is derived from pivalic acid, 3,3,3-trifluoro-2-methyl-2-(trifluoromethyl)propanoic acid, 3,3,3-trifluoro-2,2-bis(trifluoromethyl)propanoic acid, and 2,2-difluoro-2-phenylacetic acid. 10. Process according to claim 1 , wherein the process is carried out under a (partial) pressure of oxygen of 0.2-2 bar, and wherein a catalyst system is used comprising a palladium salt comprising at least one non-cyclopalladatable carboxylate anion derived from a carboxylic acid with an acidity constant in between that of acetic acid and 2,2,2-trifluoroacetic acid, with aforementioned acidity constant meaning the acidity constant average (pK a acid 1 +pK a acid 2 )/2 in case of two different carboxylate anions. 11. Process according to claim 10 , wherein the carboxylate anion is derived from 2,2-difluoroacetic acid, 2,2-difluoropropionic acid, 3,3,3-trifluoro-2-methyl-2-(trifluoromethyl)propanoic acid, 3,3,3-trifluoro-2,2-bis(trifluoromethyl)propanoic acid, 2,3,4,5,6-pentafluorobenzoic acid, 2,2-difluoro-2-phenylacetic acid, 2-(2,3,4,5,6-pentafluorophenyl)acetic acid 2,4-dinitrobenzoic acid, 2,5-dinitrobenzoic acid, and 3,4-dinitrobenzoic acid. 12. Process according to claim 1 , wherein the process is carried out under a (partial) pressure of oxygen of 2-20 bar, and wherein a catalyst system is used comprising a palladium salt comprising at least one non-cyclopalladatable carboxylate anion derived from a strongly acidic carboxylic acid, i.e. with an acidity constant that is equal or less than the acidity constant average of acetic acid and 2,2,2-trifluoroacetic acid, with aforementioned acidity constant average being quantified as (pK a acetic acid +pK a trifluoroacetic acid )/2. 13. Process according to claim 12 , wherein the carboxylate anion is derived from trifluoroacetic acid, 3,3,3-trifluoro-2,2-bis(trifluoromethyl)propanoic acid, 3,3,3-trifluoro-2-(trifluoromethyl)propanoic acid, and 2,2-difluoro-2-phenylacetic acid. 14. Process according to claim 1 , wherein at most 50 wt % of solvent is used, based on the total reaction mass. 15. Process according to claim 1 , wherein at most 10 wt % of solvent is used, based on the total reaction mass.
Organic complexes · CPC title
Complexes without C-metal linkages · CPC title
catalytic · CPC title
Substitution · CPC title
Palladium · CPC title
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