Catalyst metal separation from saturated aliphatic monocarboxylic acids

Claim 2

A process for separating manganese and copper from organic saturated aliphatic monocarboxylic acids having 6 to 9 carbon atoms which comprises treating said manganese- and copper-containing organic acids with an aqueous solution of oxalic acid in an amount sufficient to precipitate substantially all of the copper and manganese present as the oxalates from the organic acid phase into the aqueous phase, and decanting said organic acid phase from said aqueous phase.

Claim 3

The process of claim 1 wherein the volume ratio of organic acid to water ranges from about 0.5/1 to 5/1.

Claim 4

The process of claim 1 wherein the volume ratio of organic acid to water ranges from 2.5 to 1 to 1.1 to 1.

Claim 5

The process of claim 3 wherein the volume ratio of organic acid to water ranges from 1.1 to 1.7.

Claim 6

The process of claim 4 wherein at least 2% more than the stoichiometric amount of oxalic acid necessary to precipitate the copper and manganese present as the oxalates is used.

Claim 7

The process of claim 3 wherein precipitated manganese oxalate and cupric oxalate are separated from said aqueous phase and the water from said aqueous phase is then reused in the separation process.

Claim 8

The process of claim 5 wherein the organic saturated aliphatic monocarboxylic acids comprise heptanoic acid.

Claim 9

The process of claim 5 wherein the organic saturated aliphatic monocarboxylic acids comprise nonanoic acid.

Claim 10

In a process for producing organic saturated aliphatic monocarboxylic acids having 6 to 9 carbon atoms from their corresponding aldehydes by oxidizing said aldehydes in the presence of soluble manganese and copper compounds as catalysts, the improvement which comprises separating manganese and copper from said organic saturated aliphatic monocarboxylic acids by treating said organic acids which an aqueous solution of oxalic acid, the volume ratio of said organic acid to water being in the range from 0.5 to 1 to 5 to 1 and the amount of oxalic acid present being sufficient to precipitate substantially all of the copper and manganese as cupric oxalate and manganese oxalate, respectively, to precipitate said oxalates from said organic acids into the aqueous phase, and decanting said organic acids from said aqueous phase.

Claim 11

In a process for producing organic saturated aliphatic monocarboxylic acids having 6 to 9 carbon atoms from their corresponding aldehydes by oxidizing said aldehydes in the presence of soluble manganese and copper compounds as catalysts, the improvement which comprises separating manganese and copper from said organic saturated aliphatic monocarboxylic acids by treating said organic acids which an aqueous solution of oxalic acid, the volume ratio of said organic acid to water being in the range from 0.5 to 1 to 5 to 1 and the amount of oxalic acid present being sufficient to precipitate substantially all of the copper and manganese as cupric oxalate and manganese oxalate, respectively, to precipitate said oxalates from said organic acids into the aqueous phase, and decanting said organic acids from said aqueous phase.

Claim 12

The process of claim 9 wherein the volume ratio of said organic acids to water ranges from 2.5 to 1 to 1.1 to 1 and at least about 2% more than the stoichiometric amount of oxalic acid necessary to precipitate the copper and manganese present as the oxalates is used.

Claim 13

The process of claim 10 wherein said organic acids comprise heptanoic acid.

Claim 14

The process of claim 10 wherein said organic acids comprise nonanoic acid.