Liquid/liquid extraction of gallium values from basic aqueous solutions thereof

Claim 2

In a process for recovering gallium values contained in a basic aqueous solution by a liquid/liquid extraction comprising contacting the basic aqueous solution with a water immiscible organic phase comprising an organic solvent and dissolved therein an organic-soluble substituted hydroxyquinoline, whereby the gallium is extracted into the organic phase; separating the organic phase from the basic aqueous solution and recovering the gallium values from the organic phase, the improvement which comprises the organic phase further comprising dissolved therein an organic carboxylic acid compound.

Claim 3

The process as defined in claim 1, wherein the organic solvent is selected from the group consisting of heptane, petroleum fractions of the type of kerosene, benzene, toluene, xylene, chloroform, carbon tetrachloride, aromatic fractions, and mixtures thereof.

Claim 4

The process as defined in claim 1, wherein the organic-solvent-soluble substituted hydroxyquinoline is more soluble in the organic phase than in the basic aqueous phase.

Claim 5

The process as defined in claim 3, wherein the substituted hydroxyquinoline is a hydroxyquinoline which forms a complex with the gallium.

Claim 6

The process as defined in claim 3, wherein the hydroxyquinoline has the formula ##STR14## wherein R 1 , R 2 , R 3 , R 4 , R 5 and R 6 which may be the same or different from each other, each represent hydrogen or a hydrocarbon group selected from the group consisting of alkyl, alkenyl, cycloaliphatic and aromatic groups which hydrocarbon group is unsubstituted or substituted with the proviso that not all of R 1 , R 2 , R 3 , R 4 , R 5 or R 6 represent H.

Claim 7

The process as defined in claim 4, wherein the hydroxyquinoline is selected from the group consisting of α-alkenyl hydroxy-8-quinolines of the formula ##STR15## wherein R 7 , R 8 and R 9 represent hydrogen or a hydrocarbon group, which is unsubstituted or substituted, β-alkenyl hydroxy-8-quinolines of the formula ##STR16## wherein R 7 , R 8 , R 10 , R 11 , R 12 represent a hydrogen or a hydrocarbon group which is unsubstituted or substituted, and alkyl hydroxy-8-quinolines of the formula ##STR17## wherein n is comprised between 1 and 20.

Claim 8

The process as defined in claim 1, the organic phase comprises an amount of the substituted hydroxyquinoline of between about 1 and about 50% by volume relative to the volume of the organic phase.

Claim 9

The process as defined in claim 1, wherein the organic carboxylic acid compound is more soluble in the organic phase than in the aqueous phase and is selected from the group consisting of aliphatic and aromatic carboxylic acid compounds which are unsubstituted or substituted.

Claim 10

The process as defined in claim 8, wherein the organic carboxylic acid compound is selected from the group consisting of aliphatic carboxylic acids wherein the hydrocarbon moiety contains from about 3 to about 20 carbon atoms, halogenated aliphatic, aromatic or cycloaliphatic carboxylic acids, naphthenic acids of the formula ##STR18## wherein n≧1, heavy acid comprising mixtures of C 5 -C 6 , C 7 -C 9 , C 9 -C 11 , C 10 -C 16 , C 10 -C 13 , and C 12 -C 16 carboxylic acids diacids of the formula ##STR19## wherein n≧1, thioglycolic acids of the formula R--S--CH 2 --COOH wherein R is an aliphatic, cycloaliphatic, aromatic group or a combination of said groups, an acid of the formula ##STR20## wherein R 13 and R 14 are substituted or nonsubstituted hydrocarbon groups and mixtures thereof.

Claim 11

The process as defined in claim 9, wherein the organic carboxylic acid compound comprises at least one carboxylic acid group and is selected from the group consisting of butanoic acid, valeric acid, octoic acid, caprilic acid, capric acid, pelargonic acid, lauric acid alpha bromolauric acid, naphthenic acid, an acid of the formula of ##STR21## wherein R 13 is hexyl and R 14 is octyl or R 1 and R 2 each are hydrocarbon groups which together contain a total number of 7 carbon atoms and a mixture of acids of the same formula 19 wherein R 13 and R 14 are hydrocarbon groups which together contain a total number of carbon atoms of from 6 to 8.

Claim 12

The process as defined in claim 10, wherein the organic phase comprises an amount of the organic carboxylic acid of less than 20% by volume relative to the volume of the organic phase.

Claim 13

The process according to claim 11, the amount of carboxylic acid is comprised between 0 and about 10% by volume relative to the volume of the organic phase.

Claim 14

The process as defined in claim 1, wherein the organic phase further comprises a modifying agent selected from the group consisting of alcohols, phosphoric esters, phosphine esters and sulfoxides.

Claim 15

The process as defined in claim 13, wherein the modifying agent is selected from the group consisting of alcohols having between about 4 and about 15 carbon atoms and tri-butyl phosphate.

Claim 16

The process as defined in claim 1, which is performed in an inert atmosphere.

Claim 17

The process as defined by claim 1, which includes the steps of: [i] contacting the aqueous basic solution with the organic phase, whereby gallium values are extracted from the basic aqueous solution into the organic phase; [ii] separating the organic phase from the basic aqueous phase; [iii] contacting the organic phase at least once with an aqueous solution of a strong acid, to extract the gallium values from the organic phase, into the aqueous acid solution; [iv] separating the organic phase from the aqueous acid solution; and [v] separating the gallium values from the aqueous acid solution.

Claim 18

The method as defined by claim 16, in which the acid is selected from the group consisting of hydrochloric, sulfuric, nitric acid, hydrobromic acid and perchloric acid.