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Solvent-extraction process for recovery and separation of metal values

Assignee: King Industries Inc
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Filing: 1978-03-31
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Granted: 1979-09-04
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Expires: 1998-03-31
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Abstract

Abstract The metal value separation efficiencies of alkyl aromatic sulfonic acid in solvent-extraction processes are enhanced by the addition to the solvent-extractant of a fused ring aromatic N-alkyl triazole and, optionally, an aliphatic alpha -hydroxy oxime. Especially important applications for the improved solvent-extractant are in the separation and recovery of copper from iron, cobalt from nickel, copper from cobalt, cobalt from zinc, nickel from zinc, zinc from iron, nickel from iron, copper from nickel, copper from iron and copper fron zinc.

Inventors

  • 👤 Lawrence V. Gallacher
  • 👤 Rachelle M. Rydzik

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 16:43
CPC Classifications
C; C22; C22B; C22B3/00; C22B3/20; C22B3/26; C22B3/40; C22B3/406; Y; Y02; Y02P; Y02P10/00; Y02P10/20

Claims Analysis

Total Claims: 20
Claim 1
Independent Claim 184 words
A process for recovering a first cationic metal value from an aqueous solution comprising a pair of said first cationic metal value and a second cationic metal value, said pair being selected from the group consisting of copper (II) and iron, cobalt (II) and nickel, copper (II) and cobalt (II), cobalt (II) and zinc, nickel and zinc, zinc and iron, nickel and iron, copper (II) and nickel, copper (II) and iron, and copper (II) and zinc, said process comprising contacting said aqueous solution at a pH of below 3.5 with a solvent extractant consisting of (i) an alkyl aromatic sulfonic acid having a molecular weight of at least about 400, (ii) a fuzed ring aromatic N-alkyl triazole and (iii) a water-immiscible solvent for (i) and (ii) and metal complexes thereof to provide a solution of said metal-value in said solvent-extractant, the mole % of (ii) in the combined (i) and (ii) being in the range of 10 to 95; separating the solution thus formed from the aqueous raffinate depleted in said first metal value; and recovering said first metal value from said separated solution.
Claim 2
Dependent Claim 184 words
A process for recovering a first cationic metal value from an aqueous solution comprising a pair of said first cationic metal value and a second cationic metal value, said pair being selected from the group consisting of copper (II) and iron, cobalt (II) and nickel, copper (II) and cobalt (II), cobalt (II) and zinc, nickel and zinc, zinc and iron, nickel and iron, copper (II) and nickel, copper (II) and iron, and copper (II) and zinc, said process comprising contacting said aqueous solution at a pH of below 3.5 with a solvent extractant consisting of (i) an alkyl aromatic sulfonic acid having a molecular weight of at least about 400, (ii) a fuzed ring aromatic N-alkyl triazole and (iii) a water-immiscible solvent for (i) and (ii) and metal complexes thereof to provide a solution of said metal-value in said solvent-extractant, the mole % of (ii) in the combined (i) and (ii) being in the range of 10 to 95; separating the solution thus formed from the aqueous raffinate depleted in said first metal value; and recovering said first metal value from said separated solution.
Claim 3
Dependent Claim 20 words
A process as defined in claim 1 wherein said alkyl aromatic sulfonic acid (i) is a polyalkyl aromatic sulfonic acid.
Claim 4
Dependent Claim 15 words
A process as defined in claim 2 wherein said sulfonic acid is dinonylnaphthalene sulfonic acid.
Claim 5
Dependent Claim 15 words
A process as defined in claim 2 wherein said sulfonic acid is didodecylnaphthalene sulfonic acid.
Claim 6
Dependent Claim 17 words
A process as defined in claim 1 wherein said fuzed ring aromatic N-alkyl triazole (ii) is N-nonylbenzotriazole.
Claim 7
Dependent Claim 16 words
A process as defined in claim 1 wherein said fuzed ring aromatic N-alkyltriazole (ii) is N-dodecylbenzotriazole.
Claim 8
Dependent Claim 21 words
A process as defined in claim 1 wherein said first metal value is recovered from said separated solution by acid stripping.
Claim 9
Dependent Claim 16 words
A process as defined in claim 1 wherein said metal pair comprises copper (II) and iron.
Claim 10
Dependent Claim 78 words
A process as defined in claim 1 wherein said solvent-extractant also includes (iv) an aliphatic α-hydroxy oxime of the formula ##STR4## wherein R and R' are aliphatic hydrocarbon radicals and R" is hydrogen or an aliphatic hydrocarbon radical, the mole % of (i) in the combined (i) and (iv) being in the range of 10 to 95, and the mole % of (ii) in the combined (i), (ii) and (iv) being in the range of 10 to 95.
Claim 11
Dependent Claim 14 words
A process as defined in claim 9 wherein said aliphatic α-hydroxyoxime comprises 5,8-diethyl-7-hydroxydodecan-6-one oxime.
Claim 12
Dependent Claim 16 words
A process as defined in claim 9 wherein said metal pair comprises cobalt (II) and nickel.
Claim 13
Dependent Claim 16 words
A process as defined in claim 9 wherein said metal pair comprises copper (II) and cobalt.
Claim 14
Dependent Claim 16 words
A process as defined in claim 9 wherein said metal pair comprises cobalt (II) and zinc.
Claim 15
Dependent Claim 15 words
A process as defined in claim 9 wherein said metal pair comprises nickel and zinc.
Claim 16
Dependent Claim 15 words
A process as defined in claim 9 wherein said metal pair comprises zinc and iron.
Claim 17
Dependent Claim 15 words
A process as defined in claim 9 wherein said metal pair comrises nickel and iron.
Claim 18
Dependent Claim 16 words
A process as defined in claim 9 wherein said metal pair comprises copper (II) and nickel.
Claim 19
Dependent Claim 16 words
A process as defined in claim 9 wherein said metal pair comprises copper (II) and iron.
Claim 20
Dependent Claim 16 words
A process as defined in claim 9 wherein said metal pair comprises copper (II) and zinc.

References Cited (Backward Citations)

US3837964A Cited
US3872209A Cited
US3878286A Cited
US3843667A Cited
US4039612A Cited
US4018865A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-09-03 1983-03-05 1983-09-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-09-03 1987-03-05 1987-09-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-09-03 1991-03-05 1991-09-04 $7700.00 Window Closed / Lapsed

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