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US3880653A Expired / Lapsed US ⏱️ 0.0 years remaining

Chlorine leach process

Assignee: Glencore Canada Corp
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Filing: 1971-03-18
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Granted: 1975-04-29
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Expires: 1991-03-18
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Abstract

Abstract A method for selectively recovering metals from generally sulphidic particulate materials containing metals selected from nickel, copper and precious metals in which the particulate material is preferentially leached in an agitated chloride solution containing cuprous ions by the action of chlorine. The redox potential of the solution increases upon feeding chlorine thereto and decreases upon feeding particulate material thereto, and the rate of feeding of chlorine is controlled relative to the rate of feeding of material to control the redox potential substantially at or below a selected potential at which the metal is leached preferentially with respect to other metals in the material. Nickel is leached preferentially with respect to copper and precious metals in a matte, for example, to produce a nickelrich solution and to concentrate the precious metals in a nickeldepleted residue. The leach residue, or other concentrates containing copper and precious metals may also be treated by the method to selectively dissolve the copper values preferentially to the precious metal values. Dissolved copper in the nickelbearing leach solutions may be precipitated in a separate tank by agitating the leach solution in the presence of elemental sulphur and nickel sulphide particles having an atomic ratio of nickel to sulphur greater than one, thereby producing copper sulphide and a substantially copper-free nickel-chloride solution which can be separated and the values recovered by conventional means.

Inventors

  • 👤 Leif Reidar Hougen

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 10:05
CPC Classifications
C; C22; C22B; C22B23/00; C22B23/04; C22B23/0407; C22B23/0415; C22B23/0423; C22B15/00; C22B15/0063; C22B15/0065; C22B15/0067; C22B15/0069; C22B15/0084; C22B15/0089; C22B15/0093; C22B3/00; C22B3/04; C22B3/06; C22B3/10; Y; Y02; Y02P; Y02P10/00; Y02P10/20

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 163 words
IN A PROCESS FOR RECOVERING METAL FROM SOLID PARTICLES SELECTED FROM SULPHIDES AND ALLOYS AND CONTAINING AT LEAST TWO METALS SELECTED FROM NICKEL, COPPER AND PRECIOUS METALS, BY CHLORINE LEACHING THE PARTICLES AS AN AGITATED SLURRY IN A CUPROUS ION-BEARING AQUEOUS CHLORIDE SOLUTION, THE REDOX POTENTIAL OF WHICH INCREASES UPON FEEDING CHLORINE THERETO AND DECREASES UPON FEEDING THE PARTICLES THERETO, THE IMPROVEMENT FOR LEACHING AT LEAST ONE METAL PERFERNTIALLY WITH RESPECT TO MORE NOBLE METAL IN THE SOLUTION IS CONTROLLED SUBSTANTIALLY I. CONTROLLING THE RATE OF FEEDING OF CHLORINE RELATIVE TO THE RATE OF FEEDING OF PARTICLES TO THE SOLUTION SUCH THAT THE REDOX POTENTIAL OF THE SOLUTION IS CONTROLLED SUBSTANTIALLY AT A SELECTED POTENTIAL IN THE RANGE BETWEEN 250 MV AND 550 MV AT WHICH AT LEAST ONE METAL IS LEACHED PREFERENTIALLY WITH RESPECT TO SAID MORE NOBLE METAL IN THE PARTICLES, AND, II. PRODUCING A LEACH SOLUTION CONTAINING AT LEAST ONE METAL AND A LEACH RESIDUE CONTAINING SAID MORE NOBLE METAL.
Claim 2
Dependent Claim 163 words
IN A PROCESS FOR RECOVERING METAL FROM SOLID PARTICLES SELECTED FROM SULPHIDES AND ALLOYS AND CONTAINING AT LEAST TWO METALS SELECTED FROM NICKEL, COPPER AND PRECIOUS METALS, BY CHLORINE LEACHING THE PARTICLES AS AN AGITATED SLURRY IN A CUPROUS ION-BEARING AQUEOUS CHLORIDE SOLUTION, THE REDOX POTENTIAL OF WHICH INCREASES UPON FEEDING CHLORINE THERETO AND DECREASES UPON FEEDING THE PARTICLES THERETO, THE IMPROVEMENT FOR LEACHING AT LEAST ONE METAL PERFERNTIALLY WITH RESPECT TO MORE NOBLE METAL IN THE SOLUTION IS CONTROLLED SUBSTANTIALLY I. CONTROLLING THE RATE OF FEEDING OF CHLORINE RELATIVE TO THE RATE OF FEEDING OF PARTICLES TO THE SOLUTION SUCH THAT THE REDOX POTENTIAL OF THE SOLUTION IS CONTROLLED SUBSTANTIALLY AT A SELECTED POTENTIAL IN THE RANGE BETWEEN 250 MV AND 550 MV AT WHICH AT LEAST ONE METAL IS LEACHED PREFERENTIALLY WITH RESPECT TO SAID MORE NOBLE METAL IN THE PARTICLES, AND, II. PRODUCING A LEACH SOLUTION CONTAINING AT LEAST ONE METAL AND A LEACH RESIDUE CONTAINING SAID MORE NOBLE METAL.
Claim 3
Dependent Claim 56 words
Process according to claim 1 for leaching in continuous mode comprising, i. withdrawing leach solution and leach residue from the agitated slurry as particles, chlorine and solution are fed to the slurry, and ii. controlling the relative feed rates of chlorine and particles such that the redox potential is continuously maintained substantially at the selected potential.
Claim 4
Dependent Claim 54 words
Process according to claim 1 for leaching in a batch mode comprising, i. controlling the relative feed rates of chlorine and particles such that the redox potential is below the selected potential when feeding of particles is completed, and ii. continuing to feed chlorine until the redox potential has risen to the selected potential.
Claim 5
Dependent Claim 35 words
Process according to claim 2 in which the selected redox potential is within the range 250 mv to 450 mv and nickel is leached preferentially with respect to copper and precious metals in nickeliferous matte.
Claim 6
Dependent Claim 25 words
Process according to claim 3 in which copper is leached preferentially with respect to precious metals in particles selected from precious metal-bearing mattes and concentrates.
Claim 7
Dependent Claim 40 words
Process according to claim 1 comprising leaching nickel from substantially copper-free nickel matte and further comprising, iii. separating leach solution from leach residue, iv. precipitating and separating copper from the leach solution, and v. recovering nickel from the leach solution.
Claim 8
Dependent Claim 23 words
Process according to claim 6 comprising dissolving the copper precipitate and returning the dissolved copper for leaching further quantities of copper-free nickel matte.

References Cited (Backward Citations)

US2835569A Cited
US3199949A Cited
US3486847A Cited
US3627482A Cited
US3652265A Cited
US3647261A Cited
US3767760A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-04-28 1978-10-28 1979-04-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-04-28 1982-10-28 1983-04-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-04-28 1986-10-28 1987-04-29 $7700.00 Window Closed / Lapsed

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