US4000244A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Wet-chemical digestion of molybdenum sulphide containing material
Assignee: Molyscand AB
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Filing: 1975-04-30
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Granted: 1976-12-28
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Expires: 1995-04-30
Abstract
Abstract The present invention relates to a special process for the recovery of molybdenum by the wet-chemical digestion of molybdenum sulphide containing materials by means of nitric acid. The invention relates especially to the combination of a leaching procedure (that provides a very pure molybdenum oxide) and a liquid extraction procedure for the recovery of molybdenum and other values from the residual solution that is left over from the leaching procedure.
Inventors
- 👤 Bengt Olov Pontus Mollerstedt
- 👤 Karl-Erik Backius
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 17:53
CPC Classifications
C; C22; C22B; C22B34/00; C22B34/30; C22B34/34; C01; C01G; C01G39/00; C01G39/003; C01G39/02; C22B3/00; C22B3/20; C22B3/26; C22B3/28; C22B3/282; C22B61/00; C01P; C01P2006/00; C01P2006/80; Y; Y02; Y02P; Y02P10/00; Y02P10/20
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
216 words
A process for the treatment of molybdenum sulfide containing material which comprises: a. agitating together in a first leaching step molybdenum sulfide containing material with an acidic solution containing nitric acid under a temperature of 60°-120° C and pressure conditions which will enable the nitric acid to convert a substantial portion of the molybdenum sulfide to molybdic acid, b. withdrawing reaction products from said first leaching step, said reaction products being free from nitric acid, separating the reaction products of step (a) into a liquid phase and a solid phase, c. the nitric acid content of the acidic solution in step (a) being regulated so that the liquid phase resulting from step (b) is free from nitric acid, d. subjecting the liquid phase resulting from step (b) to solvent extraction with an organic solvent which is capable of dissolving therein most of the molybdenum values contained in the liquid phase resulting from step (b) e. contacting the solid phase resulting from step (b) in a second leaching step with nitric acid having an initial concentration of at least 20% in a quantity which is at least sufficient to completely oxidize all of the molybdenum sulphide in said solid phase, and f. separating the reaction products of step (e) into an acidic solution and solid molybdic acid.
Claim 2
Dependent Claim
216 words
A process for the treatment of molybdenum sulfide containing material which comprises: a. agitating together in a first leaching step molybdenum sulfide containing material with an acidic solution containing nitric acid under a temperature of 60°-120° C and pressure conditions which will enable the nitric acid to convert a substantial portion of the molybdenum sulfide to molybdic acid, b. withdrawing reaction products from said first leaching step, said reaction products being free from nitric acid, separating the reaction products of step (a) into a liquid phase and a solid phase, c. the nitric acid content of the acidic solution in step (a) being regulated so that the liquid phase resulting from step (b) is free from nitric acid, d. subjecting the liquid phase resulting from step (b) to solvent extraction with an organic solvent which is capable of dissolving therein most of the molybdenum values contained in the liquid phase resulting from step (b) e. contacting the solid phase resulting from step (b) in a second leaching step with nitric acid having an initial concentration of at least 20% in a quantity which is at least sufficient to completely oxidize all of the molybdenum sulphide in said solid phase, and f. separating the reaction products of step (e) into an acidic solution and solid molybdic acid.
Claim 3
Dependent Claim
46 words
A process for recovering molybdenum according to claim 1 characterized in that the liquid solution resulting from step (f) is used as the acidic solution for step (a) and said solvent extraction is carried out with an amine containing organic phase for recovery of residual molybdenum.
Claim 4
Dependent Claim
29 words
A process according to claim 2 characterized in that the amine containing organic phase contains at least one tertiary alkyl amine, wherein the alkyl chain has 6-20 carbon atoms.
Claim 5
Dependent Claim
30 words
A process according to claim 1 characterized in that the molybdenum sulphide containing material consists of molybdenite having a grain size within the range of from 0.2 to 0.01 mm.
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) | 1979-12-28 | 1980-06-28 | 1980-12-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-12-28 | 1984-06-28 | 1984-12-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-12-28 | 1988-06-28 | 1988-12-28 | $7700.00 | Window Closed / Lapsed |