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Extraction of metals from sea nodules

Assignee: Commissariat à l'Énergie Atomique et Aux Énergies Alternatives
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Filing: 1975-02-11
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Granted: 1977-06-14
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Expires: 1995-02-11
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Abstract

Abstract The method comprises the steps of crushing of the ore, neutralization by a mixture of water and sulphuric acid, introduction of a controlled quantity of sulphur dioxide gas at a pH value between 1.5 and 4 for promoting dissolution of nickel, copper and a desired quantity of manganese, leaching of the ore with sulphuric acid at a pH value between 1 and 3 for selectively dissolving the nickel and copper, separation of the solid and liquid phases, and separation of the metals contained in the liquid phase.

Inventors

  • 👤 Pierre Faugeras
  • 👤 Pierre Miquel
  • 👤 Michele Robaglia

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 17:08
CPC Classifications
C; C22; C22B; C22B3/00; C22B3/04; C22B3/06; C22B3/08; C22B47/00; C22B47/0018; C22B47/0045; C22B47/0054; C22B47/0063; Y; Y02; Y02P; Y02P10/00; Y02P10/20; Y10; Y10S; Y10S423/00; Y10S423/04

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 165 words
A method for extraction of metals from manganiferous sea nodules, wherein said method comprises the steps of: a. crushing of the ore; b. mixing the crushed ore with a first sulphuric acid solution to form a pulp; c. neutralizing the pulp by contact with a second sulphuric acid solution to adjust the pH of the pulp to 2 to 4, leaving substantially all the metals dissolved in the ore; d. introducing a controlled quantity of sulphur dioxide gas corresponding to the stoichiometry of the reaction of sulphation of manganese dioxide by sulphur dioxide at a pH value within the range of 1.5 to 4 with agitation in order to break down the structure of the neutralized ore and promote subsequent dissolution of the metals including the desired quantity of manganese; e. leaching the ore with sulphuric acid at a pH value within the range of 1 to 3; f. separating the solid and liquid phases; and g. separating the metals contained in the liquid phase.
Claim 2
Independent Claim 165 words
A method for extraction of metals from manganiferous sea nodules, wherein said method comprises the steps of: a. crushing of the ore; b. mixing the crushed ore with a first sulphuric acid solution to form a pulp; c. neutralizing the pulp by contact with a second sulphuric acid solution to adjust the pH of the pulp to 2 to 4, leaving substantially all the metals dissolved in the ore; d. introducing a controlled quantity of sulphur dioxide gas corresponding to the stoichiometry of the reaction of sulphation of manganese dioxide by sulphur dioxide at a pH value within the range of 1.5 to 4 with agitation in order to break down the structure of the neutralized ore and promote subsequent dissolution of the metals including the desired quantity of manganese; e. leaching the ore with sulphuric acid at a pH value within the range of 1 to 3; f. separating the solid and liquid phases; and g. separating the metals contained in the liquid phase.
Claim 3
Dependent Claim 50 words
A method of extraction according to claim 1, wherein the sulphuric acid leaching process is carried out with sulphuric acid having a pH value within the range of 1.5 to 2 at a temperature within the range of 35° to 90° C for a period of 2 to 12 hours.
Claim 4
Dependent Claim 59 words
A method of extraction according to claim 1, wherein the solution obtained on completion of step (e) is contacted with a β-alkenyl-8-hydroxyquinoline or a hydroxy-substituted oxime liquid ion exchanger to extract copper and subsequently stripping the copper from the liquid ion exchanger by contacting with a solution of copper sulphate and sulphuric acid derived from the electrolysis of copper.
Claim 5
Dependent Claim 89 words
A method of extraction according to claim 3 wherein the liquid discharged from the exchanger and no longer containing copper receives an addition of lime between 50° and 60° C at a pH equal to 3.3 in order to produce partial precipitation of iron, gallium, aluminum, chromium and is then contacted with a solvent containing 20% Di-2-ethylhexyl phosphoric acid, 5% tributyl phosphate and 75% of an aromatic solvent in order to extract the remaining iron and aluminum as well as the zinc, the rare earths and the other impurities.
Claim 6
Dependent Claim 37 words
A method of extraction according to claim 4, wherein the liquid derived from the solvent extraction process is extracted with a mixture containing a hydroxy-substituted oxime or a β-alkenyl-8-hydroxyquinoline and a naphthenic carboxylic acid to extract cobalt.
Claim 7
Dependent Claim 37 words
A method of extraction according to claim 5, wherein said method consists in contacting the liquid freed from cobalt having a pH value equal to 4 with a β-alkenyl-8-hydroxyquinoline or a hydroxy-substituted oxime to extract the nickel.
Claim 8
Dependent Claim 42 words
A method of extraction according to claim 6, wherein said method consists in oxidizing the liquid freed from nickel having a pH value equal to 8.5 in order to separate the manganese in the form of a precipitate of MnO 2 .
Claim 9
Dependent Claim 22 words
The method of extraction of claim 1 wherein the pH of the second sulphuric acid solution added for neutralization is about 2.

References Cited (Backward Citations)

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US2584700A Cited
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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) 1980-06-13 1980-12-13 1981-06-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-06-13 1984-12-13 1985-06-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-06-13 1988-12-13 1989-06-14 $7700.00 Window Closed / Lapsed

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