Claims
- 1. In a process for the recovery of copper from an aqueous ammoniacal solution containing copper values comprising:
- (A) contacting a copper pregnant aqueous ammoniacal solution containing copper values with an organic solution comprised of an insoluble beta-diketone copper extractant dissolved in a water-immiscible organic solvent to extract copper values from said aqueous ammoniacal solution into said organic solution thereby forming a copper pregnant organic phase and a copper barren aqueous phase;
- (B) separating said aqueous phase and said organic phase;
- (C) contacting the copper pregnant organic phase with an aqueous acidic stripping solution whereby copper values are stripped from the organic phase into said aqueous acidic stripping solution;
- (D) separating said aqueous acidic stripping solution, now containing the copper values from the organic phase; and
- (E) recovering the copper from the aqueous acidic stripping solution;
- wherein stripping kinetics are improved by incorporating into, or adding to the diketone extractant, an hydroxy oxime in a catalytic amount of about 0.5 to about 5 mole % relative to the diketone extractant.
- 2. A process as defined in claim 1, wherein said diketone is 1-phenyl-3-heptyl-1,3-propane dione.
- 3. A process as defined in claim 1, wherein said oxime is selected from the group consisting of dodecylsalicylaldoxime and 5,8-diethyl-7-hydroxydodecan-6-oxime.
- 4. A process as defined in claim 1, wherein said oxime has the formula: ##STR3## where R.sup.1 is a saturated aliphatic group of 1-25 carbon atoms or an ethylenically unsaturated group of 3-25 carbon atoms or OR.sub.3 where R.sup.3 is a saturated or ethylenically unsaturated group as defined above, a is an integer of 0, 1, 2, 3 or 4 and R.sup.2 is H or a saturated or ethylenically unsaturated group as defined above, with the proviso that the total number of carbon atoms in R.sup.1 and R.sup.2 is from 3-25, or is phenyl or R.sup.4 substituted phenyl, where R.sup.4 is a saturated or ethylenically unsaturated group as defined above, which may be the same or different from R.sup.1.
- 5. A process as defined in claim 4, wherein said oxime is an alkyl salicylaldoxime in which the alkyl group is selected from the group consisting of heptyl, octyl, nonyl and dodecyl.
- 6. A process as defined in claim 4, wherein the oxime is a ketoxime selected from the group consisting of 5-nonyl-2-hydroxy acetophenone oxime, 5-dodecyl-2-hydroxyacetophenone oxime, 2-hydroxy-5-nonyl benzophenone oxime and 2-hydroxy-5-dodecyl benzophenone oxime.
- 7. A copper extractant composition adapted for extracting copper values from aqueous ammoniacal copper containing solutions comprising a mixture of a diketone copper extractant and an hydroxyl oxime in a catalytic amount of about 0.5 to about 5 mole % relative to the diketone extractant.
- 8. A copper extractant composition as defined in claim 7 in which said diketone is 1-phenyl-3-heptyl-1,3-propane dione.
- 9. A copper extractant composition as defined in claim 7, wherein said oxime is selected from the group consisting of dodecylsalicylaldoxime and 5,8-diethyl-7-hydroxydodecan-6-oxime.
- 10. A copper extractant composition as defined in claim 7, wherein said oxime has the formula: ##STR4## where R.sup.1 is a saturated aliphatic group of 1-25 carbon atoms or an ethylenically unsaturated group of 3-25 carbon atoms or oR.sup.3 where R.sup.3 is a saturated or ethylenically unsaturated group as defined above, a is an integer of 0, 1, 2, 3 or 4 and R.sup.2 is H or a saturated or ethylenically unsaturated group as defined above, with the proviso that the total number of carbon atoms in R.sup.1 and R.sup.2 is from 3-25, or is phenyl or R.sup.4 substituted phenyl, where R.sup.4 is a saturated or ethylenically unsaturated group as defined above, which may be the same or different from R.sup.1.
- 11. A copper extractant composition as defined in claim 10, wherein said oxime is an alkyl salicylaldoxime in which the alkyl group is selected from the group consisting of heptyl, octyl, nonyl and dodecyl.
- 12. A copper extractant as defined in claim 10, wherein said oxime is selected from the group consisting of 5-nonyl-2-hydroxyacetophenone oxime, 5-dodecyl-2-hydroxyacetophenone oxime, 5-dodecyl-2-hydroxyacetophenone oxime, 2-hydroxy-5-nonyl benzophenone oxime and 2-hydroxy-5-dodecyl benzophenone oxime.
CROSS-REFERENCE TO RELATED APPLICATIONS
This application claims priority from U.S. provisional application Ser. No. 60/003,341, filed Sep. 7, 1995, the disclosure of which is incorporated herein by reference.
US Referenced Citations (9)
Non-Patent Literature Citations (2)
Entry |
Kuhn and Arbiter, "Physical and Chemical Separations via the Arbiter Process", 11th Int'l Mining Congress, Apr., 1975, Cagliari, Italy; Proc.--Int. Miner. Process. Congress., Paper 30; pp. 831-847. |
Kuhn and Arbiter, "Anaconda's Arbiter Process for Copper", Hydrometallurgy, CIM Bulletin, Feb., 1974. |