US4104359A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Regeneration of organic extractants containing α-hydroxyoximes
Assignee: Cyprus Amax Minerals Co
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Filing: 1977-02-28
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Granted: 1978-08-01
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Expires: 1997-02-28
Abstract
Abstract An organic liquid extractant of at least one oxime, selected from the group consisting of ketoximes and α-hydroxyoximes dissolved in an organic solvent, useful in separating nickel from cobalt in process solutions or in recovering both nickel and cobalt from process solutions, is treated with a salt of hydroxylamine at intervals to maintain the activity of the oxime in the extractant. The organic extractant can also contain sulfonic acids to facilitate treatment of more acid process solutions and is treated with a hydroxylamine salt to regenerate oxime degraded by the highly acid process solutions, the extractant itself and the concentrated acidic stripping solutions.
Inventors
- 👤 Phillip K. Davis
- 👤 Helen S. Leaver
- 👤 Henry Freiser
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 20:32
CPC Classifications
C; C22; C22B; C22B3/00; C22B3/20; C22B3/26; C22B3/30; C22B3/40; C22B3/402; C22B3/409; Y; Y02; Y02P; Y02P10/00; Y02P10/20; Y10; Y10S; Y10S423/00; Y10S423/09; Y10S423/14
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
157 words
A process for extracting at least one metal selected from the group consisting of cobalt and nickel from an acidic aqueous process solution which comprises maintaining the process solution at a temperature between about 10° C and about 40° C; contacting the process solution with a liquid extractant of at least one oxime selected from the group consisting of α-hydroxyoximes or a ketoxime which ketoxime has its oxime in the anticonfiguration with respect to the hydroxyl group and at least one sulfonic acid dissolved in a water immiscible organic solvent to load the organic extractant with the metal value; stripping the metal value from the loaded extractant with a concentrated aqueous solution of an inorganic acid to regenerate the organic extractant, recycling the regenerated extractant to the metal loading step and regenerating the organic extractant when its capacity falls below about 90% of its original capacity by reacting the organic extractant with a salt of a hydroxylamine.
Claim 2
Dependent Claim
157 words
A process for extracting at least one metal selected from the group consisting of cobalt and nickel from an acidic aqueous process solution which comprises maintaining the process solution at a temperature between about 10° C and about 40° C; contacting the process solution with a liquid extractant of at least one oxime selected from the group consisting of α-hydroxyoximes or a ketoxime which ketoxime has its oxime in the anticonfiguration with respect to the hydroxyl group and at least one sulfonic acid dissolved in a water immiscible organic solvent to load the organic extractant with the metal value; stripping the metal value from the loaded extractant with a concentrated aqueous solution of an inorganic acid to regenerate the organic extractant, recycling the regenerated extractant to the metal loading step and regenerating the organic extractant when its capacity falls below about 90% of its original capacity by reacting the organic extractant with a salt of a hydroxylamine.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-07-31 | 1982-01-30 | 1982-08-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-07-31 | 1986-01-30 | 1986-08-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-07-31 | 1990-01-30 | 1990-08-01 | $7700.00 | Window Closed / Lapsed |