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US4191728A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for selective extraction of metal ions from aqueous solutions and extracting agents suitable for that purpose

Assignee: DSM BV
•
Filing: 1978-05-09
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Granted: 1980-03-04
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Expires: 1998-05-09
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Abstract

Abstract An extraction process is described for the selective separation of bivalent metal ions belonging to the group Cu, Co, Ni and Zn in aqueous solution of Cu- and Ni-ions, Cu- and Zn-ions or Cu- and Co-ions, wherein there is used as the extraction medium one or more unsaturated fatty acids, optionally in solution and/or in admixture with saturated fatty acids and an aliphatic oxime.

Inventors

  • 👤 Martinus Tels
  • 👤 Jan P. Lotens
  • 👤 Hendrikus P. M. Kivits

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 21:30
CPC Classifications
B; B01; B01D; B01D11/00; B01D11/04; B01D11/0446; B01D11/0457; C; C02; C02F; C02F1/00; C02F1/26; C22; C22B; C22B3/00; C22B3/20; C22B3/26; C22B3/30; C22B3/32; C22B3/40; C22B3/402; C22B3/404; Y; Y02; Y02P; Y02P10/00; Y02P10/20

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 204 words
In a process for the selective extraction of copper and nickel ions from aqueous solution using a substantially immiscible organic extraction agent, the improvement wherein said extraction agent is essentially composed of a mixture of (1) oleic acid, or (2) oleic acid and at least one other unsaturated fatty acid and a (cyclo) aliphatic oxime, of from 6 to 12 carbon atoms, and wherein the (1) copper and nickel ions are first extracted with said extraction agent at a pH value of between 6 and 9 from an aqueous solution into said organic extraction agent, (2) thereafter extracting the copper and nickel ions from said organic phase into a second aqueous phase at a pH of between -2 and +1, and thereafter, (3) at a pH of between 4.0 and 6.0, selectively extracting said copper ions from said second aqueous phase with an extraction agent essentially composed of a mixture of (1) oleic acid, or (2) oleic acid and at least one other unsaturated fatty acid and a (cyclo) aliphatic oxime, of from 6 to 12 carbon atoms, and then (4) the copper ions in the organic phase are again reabsorbed into a third aqueous phase at a pH of between -2 and +1.
Claim 2
Dependent Claim 204 words
In a process for the selective extraction of copper and nickel ions from aqueous solution using a substantially immiscible organic extraction agent, the improvement wherein said extraction agent is essentially composed of a mixture of (1) oleic acid, or (2) oleic acid and at least one other unsaturated fatty acid and a (cyclo) aliphatic oxime, of from 6 to 12 carbon atoms, and wherein the (1) copper and nickel ions are first extracted with said extraction agent at a pH value of between 6 and 9 from an aqueous solution into said organic extraction agent, (2) thereafter extracting the copper and nickel ions from said organic phase into a second aqueous phase at a pH of between -2 and +1, and thereafter, (3) at a pH of between 4.0 and 6.0, selectively extracting said copper ions from said second aqueous phase with an extraction agent essentially composed of a mixture of (1) oleic acid, or (2) oleic acid and at least one other unsaturated fatty acid and a (cyclo) aliphatic oxime, of from 6 to 12 carbon atoms, and then (4) the copper ions in the organic phase are again reabsorbed into a third aqueous phase at a pH of between -2 and +1.
Claim 3
Dependent Claim 16 words
The process according to claim 1, wherein said mixture contains at least 50% of oleic acid.
Claim 4
Dependent Claim 18 words
The process according to claim 1, wherein linoleic acid or linolenic acid is present in the extraction agent.
Claim 5
Dependent Claim 12 words
The process according to claim 1, wherein the oxime is cyclohexanone oxime.
Claim 6
Dependent Claim 18 words
The process according to claim 1, wherein the fatty acid/oxime weight ratio lies between about 0.5 and 500.
Claim 7
Dependent Claim 18 words
The process according to claim 5, wherein the fatty acid/oxime weight ratio lies between about 0.5 and 50.

References Cited (Backward Citations)

US3558288A Cited
US3666446A Cited
US3703573A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-03-04 1983-09-03 1984-03-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-03-04 1987-09-03 1988-03-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-03-04 1991-09-03 1992-03-04 $7700.00 Window Closed / Lapsed

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