US4452762A
Expired / Lapsed
US
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Hydrometallurgical process for the recovery of valuable metals from metallic alloys
Assignee: Outokumpu Oyj
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Filing: 1981-06-05
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Granted: 1984-06-05
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Expires: 2001-06-05
Abstract
Abstract A process for the recovery of valuable metals from metallic alloys having iron as their principal constituent is disclosed in which the metal is leached by means of a sulfuric acid solution having such a concentration that a nearly saturated salt solution is obtained, and after the separation of a possible leach residue the solution is heated close to the boiling point, at which time an acid solution is added in an amount corresponding to the salt which has passed out of the solution, in order to crystallize the salt mixture, the crystallized material is separated from the solution and is decomposed under sulfating conditions, whereafter the metal salts are leached out from the iron oxide by means of water.
Inventors
- 👤 Sigmund P. Fugleberg
- 👤 Bror G. Nyman
- 👤 Stig-Erik Hultholm
- 👤 Asko Parviainen
- 👤 Jussi Rastas
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 01:05
CPC Classifications
C; C22; C22B; C22B7/00; C22B7/006; C22B7/007; Y; Y02; Y02P; Y02P10/00; Y02P10/20
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
209 words
A process for the recovery of iron, cobalt, nickel, molybdenum and tungsten from metallic alloys having iron as their principal constituent, comprising leaching such metal alloy in a first leaching stage with a sulfuric acid solution at a temperature of 55° to 75° C., the concentration of the acid being sufficient to produce as high a salt concentration as possible of iron, cobalt and nickel salts in solution; then raising the pH value above 2 at the end of the first leaching stage to precipitate molybdenum and tungsten values as a first leach residue; separating said first leach residue and further leaching the residue in an oxidizing alkaline leaching stage using a NaOH solution; separating molybdenum from the resulting solution by extraction by means of a suitable extractant; heating the salt solution from the first leaching stage to a temperature of 90°-105° C. and adding acid in an amount corresponding to the salt which has passed out of solution as solids, in order to crystallize salts of iron, cobalt and nickel, separating the crystallized salts from the solution, and returning the solution to the first leaching stage; decomposing the crystallized salts under sulfating conditions, and then leaching the cobalt and nickel salts from iron oxide by means of water.
Claim 2
Dependent Claim
209 words
A process for the recovery of iron, cobalt, nickel, molybdenum and tungsten from metallic alloys having iron as their principal constituent, comprising leaching such metal alloy in a first leaching stage with a sulfuric acid solution at a temperature of 55° to 75° C., the concentration of the acid being sufficient to produce as high a salt concentration as possible of iron, cobalt and nickel salts in solution; then raising the pH value above 2 at the end of the first leaching stage to precipitate molybdenum and tungsten values as a first leach residue; separating said first leach residue and further leaching the residue in an oxidizing alkaline leaching stage using a NaOH solution; separating molybdenum from the resulting solution by extraction by means of a suitable extractant; heating the salt solution from the first leaching stage to a temperature of 90°-105° C. and adding acid in an amount corresponding to the salt which has passed out of solution as solids, in order to crystallize salts of iron, cobalt and nickel, separating the crystallized salts from the solution, and returning the solution to the first leaching stage; decomposing the crystallized salts under sulfating conditions, and then leaching the cobalt and nickel salts from iron oxide by means of water.
Claim 3
Dependent Claim
35 words
The process according to claim 1, wherein the metal alloy also contains phosphorus and/or arsenic, said phosphorus and/or arsenic being precipitated along with the molybdenum and tungsten when the pH value is raised above 2.
Claim 4
Dependent Claim
26 words
The process of claim 1, in which the crystallized salts are decomposed at a temperature of 650°-700° C., in the presence of 2-15% SO 2 .
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) | 1987-06-05 | 1987-12-05 | 1988-06-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-06-05 | 1991-12-05 | 1992-06-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-06-05 | 1995-12-05 | 1996-06-05 | $7700.00 | Window Closed / Lapsed |