Process for liquid/liquid extraction of gallium

Claim 2

The process for the recovery of gallium present as a compound in solution in aqueous alkaline solutions which also contain compounds of aluminum and sodium in solution comprising contacting the aqueous solution with a water-insoluble, organic solvent-soluble substituted hydroxyquinoline in solution in a water immiscible organic solvent selected from the group consisting of halogenated and unhalogenated aliphatic and aromatic hydrocarbons whereby gallium and some of the sodium and aluminum values transfer from the aqueous phase into the organic phase, separating the organic phase from the aqueous phase, contacting the organic phase with a dilute aqueous solution of an inorganic acid to remove sodium and aluminum to the aqueous phase, leaving gallium values in solution in the organic phase, separating the organic phase from the aqueous phase, and then contacting the remaining organic phase with an aqueous solution of a more concentrated inorganic acid to remove gallium values from the organic phase to the aqueous phase, and then separating the gallium values from the aqueous phase.

Claim 3

The process as claimed in claim 1 in which the aqueous solution is a sodium aluminate solution derived from the production of alumina by the Bayer process.

Claim 4

The process as claimed in claim 1 in which an alcohol is added to the organic phase.

Claim 5

The process as claimed in claim 1 in which the sum of the carbon atoms in the substituents of the substituted hydroxyquinoline is at least 8.

Claim 6

The process as claimed in claim 1 in which the substituted hydroxyquinoline is 7 (5,5,7,7-tetramethyl 1-octene 3-yl) 8-hydroxyquinoline having the formula ##SPC2##

Claim 7

The process as claimed in claim 1 in which the amount of substituted hydroxyquinoline in the organic phase is approximately 10% by weight.

Claim 8

The process as claimed in claim 1 in which the extraction by the organic phase is carried out at a temperature below 100°C.

Claim 9

The process as claimed in claim 7 in which the temperature of extraction is within the range of 50°-80°C.

Claim 10

The process as claimed in claim 1 in which the treatment of the organic phase with the more concentrated solution of the inorganic acid to recover the gallium is carried out at a temperature below the temperature used for extraction of the aqueous solution by the organic phase.

Claim 11

The process as claimed in claim 9 in which the temperature is about ambient temperature.

Claim 12

The process for the recovery of gallium present as a compound in solution in aqueous alkaline solution which also contains compounds of aluminum and sodium in solution comprising contacting the aqueous solution with a water insoluble, organic solvent soluble substituted hydroxyquinoline in solution in a water immiscible organic solvent selected from the group consisting of halogenated and unhalogenated aliphatic and aromatic hydrocarbons whereby gallium and some of the sodium and aluminum values transfer from the aqueous phase into the organic phase, separating the organic phase from the aqueous phase, contacting the organic phase with a concentrated aqueous solution of a strong inorganic acid capable of complexing the gallium values in anionic form, which will remain in solution in the organic phase, while sodium and aluminum values transfer to the aqueous phase, separating the organic phase from the aqueous phase, and then contacting the organic phase with a dilute aqueous solution of inorganic acid to remove gallium values from the organic phase to the aqueous phase, and then separating the gallium values from the aqueous phase.

Claim 13

The process for the recovery of gallium present as a compound in solution in aqueous alkaline solution which also contains compounds of aluminum and sodium in solution comprising contacting the aqueous solution with a water insoluble, organic solvent soluble substituted hydroxyquinoline in solution in a water immiscible organic solvent selected from the group consisting of halogenated and unhalogenated aliphatic and aromatic hydrocarbons whereby gallium and some of the sodium and aluminum values transfer from the aqueous phase into the organic phase, separating the organic phase from the aqueous phase, contacting the organic phase with a concentrated aqueous solution of a strong inorganic acid capable of complexing the gallium values in anionic form, which will remain in solution in the organic phase, while sodium and aluminum values transfer to the aqueous phase, separating the organic phase from the aqueous phase, and then contacting the organic phase with a dilute aqueous solution of inorganic acid to remove gallium values from the organic phase to the aqueous phase, and then separating the gallium values from the aqueous phase.

Claim 14

The process as claimed in claim 11 in which the strong, complex forming acid is hydrochloric acid.