US4065542A
Expired / Lapsed
US
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Two stage leaching of limonitic ore and sea nodules
Assignee: Huntington Alloys Corp
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Filing: 1976-05-19
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Granted: 1977-12-27
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Expires: 1996-05-19
Abstract
Abstract A process which enables cumulative recovery of nonferrous metal values from manganiferous sea nodules and a limonitic ore comprises treating the limonitic ore in an aqueous acidic medium under reducing conditions to extract nonferrous metals and iron from the ore and form a solution containing ferrous iron and then leaching the sea nodules with such solution to extract nonferrous metals from the sea nodules and precipitate a predominant amount of the iron as hydrated ferric oxide.
Inventors
- 👤 Kohur Nagaraja Subramanian
- 👤 Gerald Vernon Glaum
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 18:31
CPC Classifications
C; C22; C22B; C22B47/00; C22B47/0018; C22B47/0045; C22B47/0054; C22B47/0063; C01; C01G; C01G49/00; C01G49/02; C01G49/06; C22B23/00; C22B23/04; C22B23/0407; C22B23/0415; C22B23/043; Y; Y10; Y10S; Y10S423/00; Y10S423/04
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
286 words
A multistage process for cumulatively extracting metal values from sea nodules containing a major amount of manganese and iron, manganese being present in tetravalent form, and containing a lesser amount of at least one of the nonferrous metals nickel, cobalt and copper, and from an iron oxide ore containing a major amount of iron and a minor amount of at least one of the nonferrous metals selected from the group nickel, cobalt and copper, iron being present in an oxidation stage higher than the divalent state, comprising: a. reductively leaching said iron oxide ore in an acidic medium in the presence of a non-oxidizing acid and a reducing agent at a temperature in the range of about 25° C to about 110° C, said acid being provided in sufficient amount to give a final pH for leaching said iron oxide ore of less than about 2 and said reducing agent being selected from the group H 2 S, FeS, ammonium sulfide, alkali metal sulfides and alkaline earth metal sulfides, to form a product comprising a first leach solution containing divalent iron and said nonferrous metal values; b. adjusting the pH of the first leach solution to at least about 3; c. selectively leaching the sea nodules in the pH-adjusted first leach solution at a temperature in the range of about 25° C to about 110° C to reduce tetravalent manganese to the divalent state and to selectively extract nonferrous metal values from the manganiferous ore into solution while precipitating iron as hydrated ferric oxide, thereby forming a second leach solution containing nonferrous metal values derived from the iron oxide ore and the sea nodules ore; and d. separating the second leach solution from the remaining residue.
Claim 2
Dependent Claim
286 words
A multistage process for cumulatively extracting metal values from sea nodules containing a major amount of manganese and iron, manganese being present in tetravalent form, and containing a lesser amount of at least one of the nonferrous metals nickel, cobalt and copper, and from an iron oxide ore containing a major amount of iron and a minor amount of at least one of the nonferrous metals selected from the group nickel, cobalt and copper, iron being present in an oxidation stage higher than the divalent state, comprising: a. reductively leaching said iron oxide ore in an acidic medium in the presence of a non-oxidizing acid and a reducing agent at a temperature in the range of about 25° C to about 110° C, said acid being provided in sufficient amount to give a final pH for leaching said iron oxide ore of less than about 2 and said reducing agent being selected from the group H 2 S, FeS, ammonium sulfide, alkali metal sulfides and alkaline earth metal sulfides, to form a product comprising a first leach solution containing divalent iron and said nonferrous metal values; b. adjusting the pH of the first leach solution to at least about 3; c. selectively leaching the sea nodules in the pH-adjusted first leach solution at a temperature in the range of about 25° C to about 110° C to reduce tetravalent manganese to the divalent state and to selectively extract nonferrous metal values from the manganiferous ore into solution while precipitating iron as hydrated ferric oxide, thereby forming a second leach solution containing nonferrous metal values derived from the iron oxide ore and the sea nodules ore; and d. separating the second leach solution from the remaining residue.
Claim 3
Dependent Claim
78 words
A process according to claim 1, wherein the reductive leach of the limonitic ore ore is carried out at a temperature between about 50° C to about 100° C at substantially atmospheric pressure and at a pH of up to about 1.5, and the selective leach of the sea nodules is carried out at a temperature between about 60° C to about 100° C, at atmospheric pressure and at an initial pH of about 3 to about 4.
Claim 4
Dependent Claim
21 words
A process according to claim 1, wherein the reducing agent for the reductive leach of the limonitic ore is hydrogen sulfide.
Claim 5
Dependent Claim
17 words
A process according to claim 1, wherein the acidic medium for the reductive leach is sulfuric acid.
Claim 6
Dependent Claim
15 words
A process according to claim 1, wherein the iron oxide ore comprises a nickeliferous limonite.
Claim 7
Dependent Claim
274 words
A multistage process for cumulatively extracting metal values from a limonitic ore and manganiferous sea nodules, said sea nodules containing a major amount of manganese and iron, manganese being predominantly in the tetravalent state, and a minor amount of nonferrous metals including at least one of the metals nickel, cobalt and copper, and said limonitic ore containing a minor amount of at least one of the nonferrous metals selected from the group nickel, cobalt and copper comprising: a. subjecting a slurry of the limonitic ore to a reductive leach in an acidic medium in the presence of a non-oxidizing acid and a reducing agent at a temperature of about 60° C to about 100° C, said acid being present in sufficient amount to give a final pH in the leach solution of up to about 1.5 said reducing agent being selected from the groups H 2 S, FeS, ammonium sulfide, alkali metal sulfides, and alkaline earth metal sulfides, to form a product comprising a first leach solution containing divalent iron and nonferrous metal values; b. adjusting the pH of the product of the limonitic ore leach to a value of between about 3 to about 4; c. forming a slurry of the manganiferous sea nodules in the pH-adjusted product at a temperature of about 50° C to about 100° C, to reduce tetravalent manganese to the divalent state and to selectively leach nonferrous metals from the nodules while precipitating iron as hydrated ferric oxide, thereby forming a second leach solution containing nonferrous metal values derived from the limonitic ore and the sea nodules; and d. separating the second leach solution from the remaining residue.
Claim 8
Dependent Claim
274 words
A multistage process for cumulatively extracting metal values from a limonitic ore and manganiferous sea nodules, said sea nodules containing a major amount of manganese and iron, manganese being predominantly in the tetravalent state, and a minor amount of nonferrous metals including at least one of the metals nickel, cobalt and copper, and said limonitic ore containing a minor amount of at least one of the nonferrous metals selected from the group nickel, cobalt and copper comprising: a. subjecting a slurry of the limonitic ore to a reductive leach in an acidic medium in the presence of a non-oxidizing acid and a reducing agent at a temperature of about 60° C to about 100° C, said acid being present in sufficient amount to give a final pH in the leach solution of up to about 1.5 said reducing agent being selected from the groups H 2 S, FeS, ammonium sulfide, alkali metal sulfides, and alkaline earth metal sulfides, to form a product comprising a first leach solution containing divalent iron and nonferrous metal values; b. adjusting the pH of the product of the limonitic ore leach to a value of between about 3 to about 4; c. forming a slurry of the manganiferous sea nodules in the pH-adjusted product at a temperature of about 50° C to about 100° C, to reduce tetravalent manganese to the divalent state and to selectively leach nonferrous metals from the nodules while precipitating iron as hydrated ferric oxide, thereby forming a second leach solution containing nonferrous metal values derived from the limonitic ore and the sea nodules; and d. separating the second leach solution from the remaining residue.
Claim 9
Dependent Claim
19 words
A process according to claim 6 wherein the acidic medium of the limonitic ore reductive leach comprises sulfuric acid.
Claim 10
Dependent Claim
19 words
A process according to claim 6 wherein the reducing agent of the limonitic ore acidic leach is hydrogen sulfide.
Claim 11
Dependent Claim
15 words
A process according to claim 6 wherein the pH adjustment is effected with calcium carbonate.
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) | 1980-12-26 | 1981-06-27 | 1981-12-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-12-26 | 1985-06-27 | 1985-12-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-12-26 | 1989-06-27 | 1989-12-27 | $7700.00 | Window Closed / Lapsed |