Solvent extraction process

Claim 2

In a solvent extraction process for recovery of copper from an aqueous feedstock solution containing dissolved copper and iron values wherein the feedstock is contacted with an organic phase comprising a reagent composition including an hydroxy aryl oxime extractant, and wherein contact between the feedstock and the organic phase is accomplished by means of countercurrent flow of feedstock and organic phase through two or more mixer-settler extraction stages, the improvement comprising: providing longer residence time for the feedstock in one or more of said mixer-settler stages wherein the feedstock initially contacts the organic phase than in one or more of the mixer-settler stages wherein the feedstock subsequently contacts the organic phase, whereby the molar ratio of copper-extractant complexes to iron-extractant complexes formed in the mixer-settler stage wherein the feedstock initially contacts the organic phase is increased and the overall copper/iron selectivity of the reagent composition is enhanced.

Claim 3

The process of claim 1 wherein the residence time of the feedstock in the mixer-settler stage wherein it initially contacts the organic phase is from 1.1 to 5.0 times longer than the retention time of the feedstock in any of one or more mixer-settler stages wherein it subsequently contacts the organic phase.

Claim 4

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 5

The process of claim 3 wherein the reagent composition comprises 2-hydroxy-5-nonyl benzaldoxime.

Claim 6

The process of claim 3 wherein the reagent composition comprises 2-hydroxy-5-dodecyl benzaldoxime.

Claim 7

The process of claim 3 wherein the reagent composition comprises 2-hydroxy-5-nonyl phenyl methyl ketone oxime.

Claim 8

In a solvent extraction process for recovery of copper from an aqueous feedstock solution containing dissolved copper and iron values wherein the feedstock is contacted with an organic phase comprising a reagent composition including a 2-hydroxy-5-dodecyl benzaldoxime extractant and wherein contact between the feedstock and the organic phase is accomplished by means of countercurrent flow of feedstock and organic phase through two or more mixer-settler extraction stages, the improvement comprising providing longer residence time for the feedstock in one or more of said mixer-settler stages wherein the feedstock initially contacts the organic phase than in one or more of the mixer-settler stages wherein the feedstock subsequently contacts the organic phase, whereby the molar ratio of copper-extractant complexes to iron-extractant complexes formed in the mixer-settler stage wherein the feedstock initially contacts the organic phase is increased and the overall copper/iron selectivity of the reagent composition is enhanced.

Claim 9

In a solvent extraction process for recovery of copper from an aqueous feedstock solution containing dissolved copper and iron values wherein the feedstock is contacted with an organic phase comprising a reagent composition including a 2-hydroxy-5-dodecyl benzaldoxime extractant and wherein contact between the feedstock and the organic phase is accomplished by means of countercurrent flow of feedstock and organic phase through two or more mixer-settler extraction stages, the improvement comprising providing longer residence time for the feedstock in one or more of said mixer-settler stages wherein the feedstock initially contacts the organic phase than in one or more of the mixer-settler stages wherein the feedstock subsequently contacts the organic phase, whereby the molar ratio of copper-extractant complexes to iron-extractant complexes formed in the mixer-settler stage wherein the feedstock initially contacts the organic phase is increased and the overall copper/iron selectivity of the reagent composition is enhanced.

Claim 10

In a solvent extraction process for recovery of copper from an aqueous feedstock solution containing dissolved copper and iron values wherein the feedstock is contacted with an organic phase comprising a reagent composition including a 2-hydroxy-5-nonyl phenyl methyl ketone oxime extractant and wherein contact between the feedstock and the organic phase is accomplished by means of countercurrent flow of feedstock and organic phase through two or more mixer-settler extraction stages, the improvement comprising providing longer residence time for the feedstock in one or more of said mixer-settler stages wherein the feedstock initially contacts the organic phase than in one or more of the mixer-settler stages wherein the feedstock subsequently contacts the organic phase, whereby the molar ratio of copper-extractant complexes to iron-extractant complexes formed in the mixer-settler stage wherein the feedstock initially contacts the organic phase is increased and the overall copper/iron selectivity of the reagent composition is enhanced.

Claim 11

In a solvent extraction process for recovery of copper from an aqueous feedstock solution containing dissolved copper and iron values wherein the feedstock is contacted with an organic phase comprising a reagent composition including a 2-hydroxy-5-nonyl phenyl methyl ketone oxime extractant and wherein contact between the feedstock and the organic phase is accomplished by means of countercurrent flow of feedstock and organic phase through two or more mixer-settler extraction stages, the improvement comprising providing longer residence time for the feedstock in one or more of said mixer-settler stages wherein the feedstock initially contacts the organic phase than in one or more of the mixer-settler stages wherein the feedstock subsequently contacts the organic phase, whereby the molar ratio of copper-extractant complexes to iron-extractant complexes formed in the mixer-settler stage wherein the feedstock initially contacts the organic phase is increased and the overall copper/iron selectivity of the reagent composition is enhanced.

Claim 12

In a solvent extraction process for recovery of copper from an aqueous feedstock solution containing dissolved copper and iron values wherein the feedstock is contacted with an organic phase comprising a reagent composition including a 2-hydroxy-5-nonyl benzaldoxime extractant and wherein contact between the feedstock and the organic phase is accomplished by means of countercurrent flow of feedstock and organic phase through two or more mixer-settler extraction stages, the improvement comprising providing longer residence time for the feedstock in one or more of said mixer-settler stages wherein the feedstock initially contacts the organic phase than in one or more of the mixer-settler stages wherein the feedstock subsequently contacts the organic phase, whereby the molar ratio of copper-extractant complexes to iron-extractant complexes formed in the mixer-settler stage wherein the feedstock initially contacts the organic phase is increased and the overall copper/iron selectivity of the reagent composition is enhanced.

Claim 13

In a solvent extraction process for recovery of copper from an aqueous feedstock solution containing dissolved copper and iron values wherein the feedstock is contacted with an organic phase comprising a reagent composition including a 2-hydroxy-5-nonyl benzaldoxime extractant and wherein contact between the feedstock and the organic phase is accomplished by means of countercurrent flow of feedstock and organic phase through two or more mixer-settler extraction stages, the improvement comprising providing longer residence time for the feedstock in one or more of said mixer-settler stages wherein the feedstock initially contacts the organic phase than in one or more of the mixer-settler stages wherein the feedstock subsequently contacts the organic phase, whereby the molar ratio of copper-extractant complexes to iron-extractant complexes formed in the mixer-settler stage wherein the feedstock initially contacts the organic phase is increased and the overall copper/iron selectivity of the reagent composition is enhanced.