Process for treatment of adipic acid mother liquor

Claim 2

In a process for the treatment of the mother liquor resulting from the nitric acid oxidation of cyclohexanol and/or cyclohexanone and the recovery of valuable components therefrom, which mother liquor contains a mixture of aliphatic dibasic acids, nitric acid and metal catalyst values, the improved process which comprises: a. contacting said mother liquor with a water-miscible lower alkyl alcohol at a temperature of from 25° C. to the boiling point of the alcohol used and in a sufficient amount to esterify at least a portion of the aliphatic dibasic acids present and form an esterifying mixture; b. contacting said esterifying mixture with a sufficient amount of a substantially water-immiscible organic solvent to extract the esters formed into said organic solvent, said organic solvent being selected from the group consisting of aromatic hydrocarbons, halogenated aliphatic hydrocarbons, halogenated aromatic hydrocarbons and mixtures thereof; c. continuing contact of said esterifying mixture and said organic solvent until at least a portion of the esters formed are partitioned into an organic phase comprising the esters dissolved in said organic solvent and there is formed said organic phase and an aqueous phase containing water, nitric acid, metal catalyst values, any excess alcohol and any unesterified organic acids; d. separating said organic phase and said aqueous phase; e. distilling said organic phase to remove the organic solvent and recover the lower alkyl esters of the aliphatic dibasic acids; f. distilling the aqueous phase to remove any excess lower alkyl alcohol and excess water; and g. recovering a residue which comprises an aqueous nitric acid solution containing metal catalyst values.

Claim 3

A process according to claim 1 wherein the mother liquor contains succinic acid, glutaric acid, adipic acid, metallic catalyst components and nitric acid.

Claim 4

A process according to claim 2 wherein the lower alkyl alcohol is a primary straight or branch chain alcohol having one to about five carbon atoms and the water-immiscible solvent is selected from the group consisting of benzene, toluene, xylene, ethylbenzene, chloroform and ortho-dichlorobenzene.

Claim 5

A process according to claim 3 wherein the mixture or organic esters is fractionally distilled to separately recover dialkyl succinate, dialkyl glutarate and dialkyl adipate.

Claim 6

In a continuous process for the treatment of the mother liquor which results from the nitric acid oxidation of cyclohexanol and/or cyclohexanone and the recovery of valuable components therefrom, which mother liquor contains a mixture of aliphatic dibasic acids, nitric acid and metal catalyst values, the improved process which comprises: a. continuously contacting said mother liquor with a water-miscible lower alkyl alcohol at a temperature of from 25° C. to the boiling point of the alcohol used and in a sufficient amount to esterify at least a portion of the dibasic acids present and form an esterifying mixture; b. continuously contacting said esterifying mixture in a countercurrent manner with a sufficient amount of a substantially water-immiscible organic solvent to extract the esters formed into said organic solvent; said organic solvent being selected from the group consisting of aromatic hydrocarbons, halogenated aliphatic hydrocarbons, halogenated aromatic hydrocarbons and mixtures thereof, said countercurrent contact being carried out by passing said esterifying mixture into at least one extractor and passing said organic solvent into at least one said extractor countercurrent to said esterifying mixture; c. continuing said countercurrent contact for a sufficient time to extract at least a portion of the esters formed into said organic solvent; d. removing the resulting mixture from the said at least one extractor, passing to at least one settler and permitting the mixture to layer out to form an organic phase and an aqueous phase, said organic phase containing esters of the aliphatic dibasic acids dissolved in said organic solvent and said aqueous phase containing water, nitric acid, metal catalyst values, any excess alcohol and any unesterified aliphatic dibasic acids; e. separating said organic phase and said aqueous phase and passing said organic phase and said aqueous phase to separate distillation stages; f. distilling said organic phase to remove organic solvent for recycle to at least one of said extractors and recovering a mixture of dialkyl esters of the aliphatic dibasic acids; g. distilling said aqueous phase to remove any excess lower alkyl alcohol and excess water and provide a residue which comprises an aqueous nitric acid solution containing metal catalyst values and any unesterified organic acids; h. recycling said residue to the nitric acid oxidation of cyclohexanol and/or cyclohexanone.

Claim 7

In a continuous process for the treatment of the mother liquor which results from the nitric acid oxidation of cyclohexanol and/or cyclohexanone and the recovery of valuable components therefrom, which mother liquor contains a mixture of aliphatic dibasic acids, nitric acid and metal catalyst values, the improved process which comprises: a. continuously contacting said mother liquor with a water-miscible lower alkyl alcohol at a temperature of from 25° C. to the boiling point of the alcohol used and in a sufficient amount to esterify at least a portion of the dibasic acids present and form an esterifying mixture; b. continuously contacting said esterifying mixture in a countercurrent manner with a sufficient amount of a substantially water-immiscible organic solvent to extract the esters formed into said organic solvent; said organic solvent being selected from the group consisting of aromatic hydrocarbons, halogenated aliphatic hydrocarbons, halogenated aromatic hydrocarbons and mixtures thereof, said countercurrent contact being carried out by passing said esterifying mixture into at least one extractor and passing said organic solvent into at least one said extractor countercurrent to said esterifying mixture; c. continuing said countercurrent contact for a sufficient time to extract at least a portion of the esters formed into said organic solvent; d. removing the resulting mixture from the said at least one extractor, passing to at least one settler and permitting the mixture to layer out to form an organic phase and an aqueous phase, said organic phase containing esters of the aliphatic dibasic acids dissolved in said organic solvent and said aqueous phase containing water, nitric acid, metal catalyst values, any excess alcohol and any unesterified aliphatic dibasic acids; e. separating said organic phase and said aqueous phase and passing said organic phase and said aqueous phase to separate distillation stages; f. distilling said organic phase to remove organic solvent for recycle to at least one of said extractors and recovering a mixture of dialkyl esters of the aliphatic dibasic acids; g. distilling said aqueous phase to remove any excess lower alkyl alcohol and excess water and provide a residue which comprises an aqueous nitric acid solution containing metal catalyst values and any unesterified organic acids; h. recycling said residue to the nitric acid oxidation of cyclohexanol and/or cyclohexanone.

Claim 8

A process according to claim 5 wherein the mother liquor contains succinic acid, glutaric acid, adipic acid, and nitric acid.

Claim 9

A process according to claim 6 wherein the esterifying alcohol is a primary straight or branch chain alcohol having one to about five carbon atoms and the water-immiscible solvent is selected from the group consisting of benzene, toluene, xylene, ethylbenzene, chloroform and ortho-dichlorobenzene.

Claim 10

A process according to claim 7 wherein the mixture of dialkyl esters of aliphatic dibasic acids recovered in step (e) is fractionally distilled to separately recover dialkyl succinate. dialkyl glutarate and dialkyl adipate.

Claim 11

A process according to claim 7 wherein the alcohol is methanol, the water-immiscible solvent is benzene, and these materials are employed in a volume equal to the volume of liquid being treated in the esterification and extraction step. pg,31

Claim 12

In a process for the treatment of the mother liquor resulting from the nitric acid oxidation of cyclohexanol and/or cyclohexanone and the recovery of valuable components therefrom, which mother liquor contains a mixture of aliphatic dibasic acids, nitric acid and metal catalyst values, the improved process which comprises: a. contacting said mother liquor with a water-miscible lower alkyl alcohol at a temperature of from 25° C. to the boiling point of the alcohol used and in a sufficient amount to esterify at least a portion of the aliphatic dibasic acids present and form an esterifying mixture; b. contacting said esterifying mixture with a sufficient amount of a substantially water-immiscible organic solvent to extract the esters formed into said organic solvent, said organic solvent being selected from the group consisting of aromatic hydrocarbons, halogenated aliphatic hydrocarbons and halogenated aromatic hydrocarbons; c. continuing contact of said esterifying mixture and said organic solvent until at least a portion of the esters formed are partitioned into an organic phase comprising the esters dissolved in said organic solvent and there is formed said organic phase and an aqueous phase containing water, nitric acid, metal catalyst values, and excess alcohol and any unesterified organic acids; d. separating said organic phase and said aqueous phase; e. distilling said organic phase to remove the organic solvent and recover the lower alkyl esters of the aliphatic dibasic acids; f. distilling the aqueous phase to remove any excess lower alkyl alcohol and excess water; g. recovering a residue which comprises an aqueous nitric acid solution containing metal catalyst values; and h. recycling the recovered residue of nitric acid solution containing metal catalyst values to the nitric acid oxidation of cyclohexanol and/or cyclohexanone.

Claim 13

In a process for the treatment of the mother liquor resulting from the nitric acid oxidation of cyclohexanol and/or cyclohexanone and the recovery of valuable components therefrom, which mother liquor contains a mixture of aliphatic dibasic acids, nitric acid and metal catalyst values, the improved process which comprises: a. contacting said mother liquor with a water-miscible lower alkyl alcohol at a temperature of from 25° C. to the boiling point of the alcohol used and in a sufficient amount to esterify at least a portion of the aliphatic dibasic acids present and form an esterifying mixture; b. contacting said esterifying mixture with a sufficient amount of a substantially water-immiscible organic solvent to extract the esters formed into said organic solvent, said organic solvent being selected from the group consisting of aromatic hydrocarbons, halogenated aliphatic hydrocarbons and halogenated aromatic hydrocarbons; c. continuing contact of said esterifying mixture and said organic solvent until at least a portion of the esters formed are partitioned into an organic phase comprising the esters dissolved in said organic solvent and there is formed said organic phase and an aqueous phase containing water, nitric acid, metal catalyst values, and excess alcohol and any unesterified organic acids; d. separating said organic phase and said aqueous phase; e. distilling said organic phase to remove the organic solvent and recover the lower alkyl esters of the aliphatic dibasic acids; f. distilling the aqueous phase to remove any excess lower alkyl alcohol and excess water; g. recovering a residue which comprises an aqueous nitric acid solution containing metal catalyst values; and h. recycling the recovered residue of nitric acid solution containing metal catalyst values to the nitric acid oxidation of cyclohexanol and/or cyclohexanone.

Claim 14

In a process for the treatment of the mother liquor resulting from the nitric acid oxidation of cyclohexanol and/or cyclohexanone and the recovery of valuable components therefrom, which mother liquor is a dilute aqueous nitric acid stream containing metal oxidation catalysts, a mixture of adipic, succinic and glutaric acids and from 6 to 20 weight percent nitric acid, the improved process which comprises: a. contacting said mother liquor with methanol at a temperature of from 25° C to the boiling point of the alcohol and in an amount sufficient to esterify said acids present and form an esterifying mixture of methyl esters; b. contacting said esterifying mixture with a sufficient amount of benzene solvent to extract the esters formed into said solvent; c. continuing contact of said esterifying mixture and benzene until at least a portion of the methyl esters formed are partitioned into an organic phase comprising the esters dissolved in benzene and there is formed said organic phase and an aqueous phase containing water, nitric acid, metal catalyst values, any excess alcohol and any unesterified organic acids; d. separating said organic phase and said aqueous phase; e. distilling said organic phase to remove benzene and recover the methyl esters of said acids; f. distilling the aqueous phase to remove any excess methanol and excess water; and g. recovering a residue which comprises an aqueous nitric acid solution containing metal catalyst values.

Claim 15

In a process for the treatment of the mother liquor resulting from the nitric acid oxidation of cyclohexanol and/or cyclohexanone and the recovery of valuable components therefrom, which mother liquor is a dilute aqueous nitric acid stream containing metal oxidation catalysts, a mixture of adipic, succinic and glutaric acids and from 6 to 20 weight percent nitric acid, the improved process which comprises: a. contacting said mother liquor with methanol at a temperature of from 25° C to the boiling point of the alcohol and in an amount sufficient to esterify said acids present and form an esterifying mixture of methyl esters; b. contacting said esterifying mixture with a sufficient amount of benzene solvent to extract the esters formed into said solvent; c. continuing contact of said esterifying mixture and benzene until at least a portion of the methyl esters formed are partitioned into an organic phase comprising the esters dissolved in benzene and there is formed said organic phase and an aqueous phase containing water, nitric acid, metal catalyst values, any excess alcohol and any unesterified organic acids; d. separating said organic phase and said aqueous phase; e. distilling said organic phase to remove benzene and recover the methyl esters of said acids; f. distilling the aqueous phase to remove any excess methanol and excess water; and g. recovering a residue which comprises an aqueous nitric acid solution containing metal catalyst values.