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US4087339A Expired / Lapsed US ⏱️ 0.0 years remaining

Electrowinning of sulfur-containing nickel

Assignee: Huntington Alloys Corp
•
Filing: 1977-01-11
•
Granted: 1978-05-02
•
Expires: 1997-01-11
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Abstract

Abstract Sulfur-containing nickel is electrodeposited from a chloride electrolyte in a cell wherein each cathode is separated from any adjacent anode by a pair of diaphragms.

Inventors

  • 👤 Robert William Elliott
  • 👤 John Ambrose
  • 👤 Victor Alexander Ettel

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 18:52
CPC Classifications
C; C25; C25C; C25C1/00; C25C1/06; C25C1/08

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 159 words
A process for producing sulfur-containing nickel comprising establishing an aqueous electrolyte which contains in solution nickel ions, chloride ions and a sulfur-bearing compound selected from the group consisting of sulfur dioxide, thiourea, toluene sulfonamide as well as sulfites, bisulfites, thiosulfates and tetrathionates of alkali and alkaline earth metals, electrodepositing nickel from said electrolyte in a cell having at least one electrode assembly, which assembly comprises an anode substantially insoluble in said electrolyte, a cathode, an anolyte diaphragm-means for isolating said anode and a volume of said electrolyte adjacent thereto from the remainder of said electrolyte within said cell and a catholyte diaphragm-means for isolating said cathode and a volume of said electrolyte adjacent thereto from the remainder of said electrolyte within said cell, and maintaining a flow of said electrolyte through said cell during electrodeposition by introducing fresh electrolyte to the interior only of said catholyte diaphragm-means and withdrawing spent electrolyte from the exterior only of said catholyte diaphragm-means.
Claim 2
Dependent Claim 159 words
A process for producing sulfur-containing nickel comprising establishing an aqueous electrolyte which contains in solution nickel ions, chloride ions and a sulfur-bearing compound selected from the group consisting of sulfur dioxide, thiourea, toluene sulfonamide as well as sulfites, bisulfites, thiosulfates and tetrathionates of alkali and alkaline earth metals, electrodepositing nickel from said electrolyte in a cell having at least one electrode assembly, which assembly comprises an anode substantially insoluble in said electrolyte, a cathode, an anolyte diaphragm-means for isolating said anode and a volume of said electrolyte adjacent thereto from the remainder of said electrolyte within said cell and a catholyte diaphragm-means for isolating said cathode and a volume of said electrolyte adjacent thereto from the remainder of said electrolyte within said cell, and maintaining a flow of said electrolyte through said cell during electrodeposition by introducing fresh electrolyte to the interior only of said catholyte diaphragm-means and withdrawing spent electrolyte from the exterior only of said catholyte diaphragm-means.
Claim 3
Dependent Claim 33 words
A process as claimed in claim 1 wherein said cell includes anode cover-means so dimensioned and positioned relative to said anolyte diaphragm-means as to define a substantially sealed space above said anolyte diaphragm-means.
Claim 4
Dependent Claim 23 words
A process as claimed in claim 2 wherein substantially all of said nickel in said electrolyte is in the form of nickel chloride.
Claim 5
Dependent Claim 16 words
A process as claimed in claim 3 wherein said sulfur-bearing compound comprises an alkali metal thiosulfate.
Claim 6
Dependent Claim 37 words
A process as claimed in claim 4 wherein said electrolyte contains about 150-255 grams per liter of nickel, up to about 20 grams per liter of boric acid and about 50-160 milligrams per liter of thiosulfate ions.
Claim 7
Dependent Claim 52 words
A process as claimed in claim 5 wherein the rate of introduction of fresh electrolyte into said cell and the rate of withdrawal of spent electrolyte therefrom are controlled so as to maintain a difference of at least 70 grams per liter between the nickel contents of said fresh and spent electrolytes.

References Cited (Backward Citations)

US2392708A Cited
US2453757A Cited
US2623848A Cited
US2480771A Cited
GB992767A Cited
US3855089A Cited
US3959111A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-05-01 1981-10-31 1982-05-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-05-01 1985-10-31 1986-05-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-05-01 1989-10-31 1990-05-02 $7700.00 Window Closed / Lapsed

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