Production of propionic acid

Claim 2

In a process for production of propionic acid, propionic anhydride and mixtures thereof with the repression of polyketones wherein ethylene is reacted, in the absence of hydrogen, with carbon monoxide and at least one member of the group consisting of water, propionic acid and mixtures thereof, at a temperature of 50° to 300°C, the improvement which comprises contacting the said reactants in the presence of a catalyst system consisting essentially of an iridium complex containing at least one ligand selected from the group consisting of a tertiary organophosphorus compound of 3 to 90 carbon atoms, a tertiary organoarsenic compound of 3 to 90 carbon atoms, a tertiary organoantimony compound of 3 to 90 carbon atoms, an olefinic compound of 2 to 40 carbon atoms, and an organo-diolefinic compound of 2 to 40 carbon atoms in the substantial absence of added halide components.

Claim 3

In a process for production of propionic acid, propionic anhydride and mixtures thereof with the repression of polyketones wherein ethylene is reacted, in the absence of hydrogen, with carbon monoxide and at least one member of the group consisting of water, propionic acid, and mixtures thereof, at a temperature of 50° to 300°C, the improvement which comprises contacting the said reactants in the presence of a catalyst system consisting essentially of an iridium complex, containing carbon monoxide, and at least one ligand selected from the group consisting of a tertiary organophosphorus compound of 3 to 90 carbon atoms, a tertiary organoarsenic compound of 3 to 90 carbon atoms, a tertiary organoantimony compound of 3 to 90 carbon atoms, an olefinic compound of 2 to 40 carbon atoms, and an organo-diolefinic compound of 2 to 40 carbon atoms in the substantial absence of added halide components.

Claim 4

In a process for production of propionic acid, propionic anhydride and mixtures thereof with the repression of polyketones wherein ethylene is reacted, in the absence of hydrogen, with carbon monoxide and at least one member of the group consisting of water, propionic acid, and mixtures thereof, at a temperature of 50° to 300°C, the improvement which comprises contacting the said reactants in the presence of a catalyst system consisting essentially of an iridium complex, containing carbon monoxide, and at least one ligand selected from the group consisting of a tertiary organophosphorus compound of 3 to 90 carbon atoms, a tertiary organoarsenic compound of 3 to 90 carbon atoms, a tertiary organoantimony compound of 3 to 90 carbon atoms, an olefinic compound of 2 to 40 carbon atoms, and an organo-diolefinic compound of 2 to 40 carbon atoms in the substantial absence of added halide components.

Claim 5

Process as in claim 1 in which the tertiary ligand is a tertiary aryl or aryloxy phosphorus compound.

Claim 6

Process as in claim 1 in which iridium complex is provided by an iridium complex in which the iridium is in the plus one, (+I), oxidation state.

Claim 7

Process as in claim 1 in which the iridium complex is provided by an iridium complex in which the iridium is in the plus, three, (+III), oxidation state.

Claim 8

Process as in claim 1 in which the atomic ratio of halogen to iridium of the iridium complex as charged to the process is from 0:1 to 2:1.

Claim 9

Process as in claim 2 in which the iridium complex is provided by hydridodicarbonylbistriphenylphosphineiridium(I).

Claim 10

Process as in claim 1 in which the catalyst system is provided by μ,μ-dichlorobis-1,5-cyclooctadienediiridium(I).

Claim 11

Process as in claim 2 in which the catalyst system is provided by chlorocarbonylbistriphenylariineiridium(I).

Claim 12

Process as in claim 2 in which the catalyst system is provided by acetatocarbonylbistriphenylphosphineiridium(I).