US4028463A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Recovery of manganese values
Assignee: Honeywell UOP LLC
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Filing: 1976-02-19
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Granted: 1977-06-07
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Expires: 1996-02-19
Abstract
Abstract Manganese values may be recovered from manganese bearing sources by subjecting said source to a roast in the presence of sulfuric acid and a reductant which comprises a chromium-containing compound at temperatures ranging from about 200° to about 500° C. followed by leaching, separation, solvent extraction or ion exchange whereby manganese is extracted, followed by separation and recovery of the manganese.
Inventors
- 👤 John C. Stauter
- 👤 Richard T. Um
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 19:46
CPC Classifications
C; C22; C22B; C22B47/00; C22B47/0018; C22B47/0027; C01; C01G; C01G45/00; C01G45/10; C22B47/0045; C22B47/0054; C22B47/0063
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
183 words
In a process for the recovery of manganese values from a manganese bearing source, the steps of: a. forming a mixture of said manganese bearing source, sulfuric acid and a reductant comprising a chromium-containing compound in a weight ratio of from about 1:1:1 to about 2:1:10 manganese bearing source, chromium-containing compound and sulfuric acid, respectively; b. roasting said mixture at a temperature of from about 200° to about 500° C. for a sufficient time to remove the major portion of its water content and excess sulfuric acid; c. leaching the resultant pulp with water at a temperature of from about 25° to about 95° C; d. filtering the leach solution to separate undissolved solids from pregnant leach liquor containing dissolved manganese ions and chromium ions; e. selectively extracting the chromium ions from said pregnant leach liquor with an organic amine solvent; and f. precipitating manganese as solid manganese sulfate from the remaining leach liquor by subjecting the latter to a pressure of from about 50 to about 500 pounds per square inch at a temperature of from about 130° to about 250° C.
Claim 2
Dependent Claim
183 words
In a process for the recovery of manganese values from a manganese bearing source, the steps of: a. forming a mixture of said manganese bearing source, sulfuric acid and a reductant comprising a chromium-containing compound in a weight ratio of from about 1:1:1 to about 2:1:10 manganese bearing source, chromium-containing compound and sulfuric acid, respectively; b. roasting said mixture at a temperature of from about 200° to about 500° C. for a sufficient time to remove the major portion of its water content and excess sulfuric acid; c. leaching the resultant pulp with water at a temperature of from about 25° to about 95° C; d. filtering the leach solution to separate undissolved solids from pregnant leach liquor containing dissolved manganese ions and chromium ions; e. selectively extracting the chromium ions from said pregnant leach liquor with an organic amine solvent; and f. precipitating manganese as solid manganese sulfate from the remaining leach liquor by subjecting the latter to a pressure of from about 50 to about 500 pounds per square inch at a temperature of from about 130° to about 250° C.
Claim 3
Dependent Claim
17 words
The process as set forth in claim 1 in which said manganese bearing source is sea nodules.
Claim 4
Dependent Claim
18 words
The process as set forth in claim 1 in which said manganese being source is manganese dioxide ore.
Claim 5
Dependent Claim
15 words
The process as set forth in claim 1 in which said reductant is chromite ore.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-06-06 | 1980-12-06 | 1981-06-07 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-06-06 | 1984-12-06 | 1985-06-07 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-06-06 | 1988-12-06 | 1989-06-07 | $7700.00 | Window Closed / Lapsed |