Solvent extraction process

Claim 2

In a solvent extraction process for recovery of copper from an aqueous feedstock containing copper and iron values wherein the feedstock is contacted with an organic phase comprising a reagent composition including an hydroxy aryl oxime extractant and in which a copper loaded organic phase is provided by extraction of said copper values from said aqueous feedstock and wherein contact between the feedstock and the organic phase is accomplished by means of at least one mixer-settler extraction stage and at least one strip stage to provide a pregnant copper electrolyte from which the copper is electrowon to provide cathode copper and a stripped electrolyte the improvement comprising washing said copper loaded organic phase prior to stripping said copper values therefrom with an aqueous scrub solution containing at least a portion of electrolyte thereby providing an increased copper to iron ratio by weight in said copper loaded organic phase.

Claim 3

A process as defined in claim 1 in which said electrolyte is present in said aqueous acidic scrub solution in an amount of from about 1-20 volume to volume percent.

Claim 4

A process as defined in claim 2 in which said electrolyte is said pregnant copper electrolyte.

Claim 5

A process as defined in claim 2 in which said electrolyte is said stripped electrolyte.

Claim 6

A process as defined in claim 1 in which said aqueous feedstock is a chloride containing feedstock.

Claim 7

A process as defined in claim 5 in which said chloride containing feedstock contains up to 50 grams per liter Cl.

Claim 8

A process as defined in claim 6 wherein said feedstock contains from 5-15 g/l Cl.

Claim 9

The process of claim 1 wherein the reagent composition comprises: (a) one or more hydroxy aryl ketone oxime compounds of Formula I or II, ##STR4## in which R and R' may be individually alike or different and are saturated aliphatic groups of 1-25 carbon atoms, ethylenically unsaturated aliphatic groups of 3-25 carbon atoms or --OR" where R" is a saturated or ethylenically unsaturated aliphatic group as defined; n is 0 or 1; and a and b are each 0, 1, 2, 3 or 4, with the proviso that both, are not 0 and the total number of carbon atoms in R a and R' b is from 3 to 25, ##STR5## in which R and a are as defined with respect to Formula I and R"' is a saturated aliphatic group of 1-25 carbon atoms or an ethylenically unsaturated aliphatic group of 3-25 carbon atoms, with the proviso that the total number of carbon atoms in R a and R"' is from 3 to 25; and/or (b) one or more hydroxy aryl aldoxime compounds of Formula III, ##STR6## in which R is as defined above with respect to Formulas I and II, c has a value of 1, 2, 3 or 4, and the total number of carbon atoms in R c is from 3 to 25.

Claim 10

The process of claim 8 wherein the reagent composition comprises 2-hydroxy-5-nonyl benzaldoxime.

Claim 11

The process of claim 8 wherein the reagent composition comprises 2-hydroxy-5-dodecyl benzaldoxime.

Claim 12

The process of claim 8 wherein the reagent composition comprises 2-hydroxy-5-nonyl phenyl methyl ketone oxime.

Claim 13

The process of claim 8 wherein the reagent composition is a mixture of 2-hydroxy-5-nonylbenzophenone oxime and 2-hydroxy-5-dodecyl benzaldoxime.

Claim 14

The process of claim 8 wherein the reagent is a mixture of 2-hydroxy-5-nonylbenzophenone oxime, 2-hydroxy-5-dodecyl benzaldoxime and 2-hydroxy-5-nonylphenyl methyl ketone oxime.

Claim 15

In a solvent extraction process for the recovery of copper from an aqueous feedstock containing copper and iron values and up to about 50 g/l Cl wherein the feedstock is contacted with an organic phase comprising a reagent composition including an hydroxy oxime extractant in which a copper loaded organic phase is provided by extraction of said copper values from said aqueous feedstock by said oxime extractant and wherein contact between the feedstock and the organic phase is accomplished by means of at least one mixer-settler extraction stage and at least one strip stage to provide a pregnant copper electrolyte from which the copper is electrowon to provide cathode copper and a stripped electrolyte the improvement comprising washing said copper loaded organic phase prior to stripping said copper values therefrom with an aqueous scrub solution containing about 1-20 v/v% of electrolyte thereby providing an increased copper to iron ratio by weight in said copper loaded organic phase.

Claim 16

In a solvent extraction process for the recovery of copper from an aqueous feedstock containing copper and iron values and up to about 50 g/l Cl wherein the feedstock is contacted with an organic phase comprising a reagent composition including an hydroxy oxime extractant in which a copper loaded organic phase is provided by extraction of said copper values from said aqueous feedstock by said oxime extractant and wherein contact between the feedstock and the organic phase is accomplished by means of at least one mixer-settler extraction stage and at least one strip stage to provide a pregnant copper electrolyte from which the copper is electrowon to provide cathode copper and a stripped electrolyte the improvement comprising washing said copper loaded organic phase prior to stripping said copper values therefrom with an aqueous scrub solution containing about 1-20 v/v% of electrolyte thereby providing an increased copper to iron ratio by weight in said copper loaded organic phase.

Claim 17

A process as defined in claim 14 in which said electrolyte is said pregnant copper electrolyte.

Claim 18

A process as defined in claim 14 in which said electrolyte is said stripped electrolyte.

Claim 19

A process as defined in claim 14 wherein said hydroxy aryl oxime extractant is selected from the group consisting of 2-hydroxy-5-nonylbenzophenone oxime, 2-hydroxy-5-dodecyl benzaldoxime, 2-hydroxy-5-nonyl benzaldoxime, 2-hydroxy-5-nonylphenyl methyl ketone oxime and mixtures thereof.