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

Claim 2

In a method for recovering gallium values contained in a basic aqueous solution by liquid/liquid extraction comprising extracting the basic aqueous solution with a water immiscible organic phase comprising an organic solvent and a dissolved, water-insoluble substituted hydroxyquinoline whereby the gallium values are transferred 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 conducting, under an inert gas atmosphere, at least the step of extraction of the gallium values.

Claim 3

The method as defined by claim 1, wherein the inert atmosphere is gaseous nitrogen.

Claim 4

The method as defined by claim 1, wherein the inert atmosphere is gaseous argon.

Claim 5

The method as defined by claim 1, wherein the very steps aqueous solutions which are extracted by means of the organic phase are sodium aluminate solutions emanating from the production of alumina by the Bayer process, and containing gallium, aluminum and sodium values.

Claim 6

The method as defined by claim 4, which includes the step of: (i) contacting the aqueous sodium aluminate solution with the organic phase, whereby gallium values and part of the amount of sodium and aluminum values are extracted from the aqueous phase to the organic phase; (ii) separating the organic phase from the aqueous phase; (iii) contacting the organic phase with a dilute aqueous solution of an acid, to extract sodium and aluminum values from the organic phase, and maintaining the gallium values in solution in the said organic phase; (iv) separating the organic from the aqueous phase and contacting the remaining organic phase with a more concentrated aqueous acid solution, to transfer the gallium values from the organic phase to the aqueous phase; and (v) separating the gallium values from the aqueous phase.

Claim 7

The method as defined by claim 5, in which the acid is selected from the group consisting of hydrochloric, sulfuric and nitric acid.

Claim 8

The method as defined by claim 5, in which the concentration of the dilute aqueous acid solution is from 0.1 M to 1 M.

Claim 9

The method as defined by claim 5, in which the concentration of the more concentrated aqueous acid solution is greater than 1 M.

Claim 10

The method as defined by claim 4, which includes the steps of: [i] contacting the aqueous sodium aluminate solution with an organic phase, whereby gallium values and a certain amount of sodium and aluminum values are extracted from the aqueous to the organic phase, and in which the organic solvent is selected from the group consisting of halogenated and non-halogenated aliphatic and aromatic hydrocarbons; [ii] separating the organic phase from the aqueous phase; [iii] contacting the organic phase with a concentrated aqueous solution of an acid capable of chelating the gallium in anionic form, the gallium values remaining in solution in the organic phase while the sodium and aluminum values are transferred into the aqueous phase; [iv] separating the organic phase from the aqueous phase and contacting the remaining organic phase with a dilute aqueous acid solution, whereby gallium values transfer from the organic to the aqueous phase; and [v] separating the gallium values from the aqueous phase.

Claim 11

The method as defined by claim 9, in which the acid is selected from the group consisting of hydrochloric and hydrobromic acid.

Claim 12

The method as defined by claim 9, in which the concentrated aqueous acid solution has a concentration of from 5 M to 8 M.

Claim 13

The method as defined by claim 9, in which the concentration of the dilute aqueous acid solution is less than 2.2 M.

Claim 14

The method as defined by claim 5, wherein the first stage in the process, the contacting of the aqueous sodium aluminate solution with the organic phase, is carried out at elevated temperature of less than 100° C.

Claim 15

The method as defined by claim 5, in which the organic phase comprising gallium values is treated with an aqueous acid solution at a temperature below that of the first stage of contacting the aluminate solution with the organic phase.

Claim 16

The method as defined by claim 14, in which the temperature used is ambient temperature.

Claim 17

The method as defined by claim 4, which includes the following steps: [i] contacting the aqueous solution with a water-insoluble substituted hydroxyquinoline in solution in a water-insoluble organic solvent selected from the group consisting of halogenated or non-halogenated aliphatic and aromatic hydrocarbons, whereby the gallium values and part of the amount of sodium and aluminum values are extracted from the aqueous phase to the organic phase; [ii] separating the organic phase from the aqueous phase; [iii] contacting the organic phase with an aqueous solution of an acid, whereby the gallium, sodium and the aluminum values in the organic phase are transferred to the aqueous phase; [iv] separating the aqueous phase from the organic phase; and [v] recovering the gallium value together with sodium and aluminum values.

Claim 18

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

Claim 19

The method as defined by claim 17, in which the concentration of the sulfuric and nitric acids is above 1.6 M.

Claim 20

The method as defined by claim 17, in which the concentration of hydrochloric and hydrobromic acids is from 1.3 to 2.2 M.

Claim 21

The method as defined by claim 9, wherein the first stage of the process, comprising contacting the aqueous sodium aluminate solution with the organic phase, said contacting is carried out at elevated temperature of less than 100° C.

Claim 22

The method as defined by claim 9, in which the organic phase containing gallium values is treated with an aqueous acid solution at a temperature below that of the first stage for contacting the aluminate solution with the organic phase.

Claim 23

The method as defined by claim 21, in which the temperature is about ambient temperature.

Claim 24

The method as defined by claim 16, wherein the first stage of the process, comprising contacting the aqueous sodium aluminate solution with the organic phase, said contacting is carried out at elevated temperature of less than 100° C.

Claim 25

The method as defined by claim 16, in which the organic phase containing gallium values is treated with an aqueous acid solution at a temperature below that of the first stage for contacting the aluminate solution with the organic phase.

Claim 26

The method as defined by claim 24, in which the temperature is about ambient temperature.

Claim 27

The method as defined by claim 1, the hydroxyquinoline having the structural formula: ##STR4## wherein each R, which may be the same or different, is selected from the group consisting of hydrogen and the alkyl group C n H 2n+1 .

Claim 28

The method as defined by claim 1, the hydroxyquinoline having the structural formula: ##STR5## wherein n is a number of from 5 to 20.

Claim 29

The method as defined by claim 1, the hydroxyquinoline having the structural formula: ##STR6##

Claim 30

The method as defined by claim 1, wherein any one or more of the liquid/liquid extraction stages, in addition to the extraction step proper of the gallium values, is conducted under an inert atmosphere.

Claim 31

The method as defined by claim 29, wherein all stages are conducted under an inert atmosphere.

Claim 32

The method as defined by claim 26, wherein n is a number of from 5 to 20.