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US3930967A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the electrolysis of a molten charge using inconsumable bi-polar electrodes

Assignee: Rio Tinto Switzerland AG
•
Filing: 1974-07-03
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Granted: 1976-01-06
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Expires: 1994-07-03
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Abstract

Abstract A process for the production of metals by the electrolysis of metal compounds dissolved in a molten electrolyte, in particular for the production of aluminum from aluminum oxide. The electric power is passed through a multi-cell furnace with at least one inconsumable bi-polar electrode, made of electrode materials which are compatible with one another. The anions, in particular, the oxygen ions of the dissolved metal compounds have their charges removed on the surface of the electron conductive ceramic oxide anode and the metal ions, in particular the aluminum ions on the surface of the cathode which is made of another material than that used for the anode surface.

Inventors

  • 👤 Hanspeter Alder

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 18:37
CPC Classifications
C; C25; C25C; C25C3/00; C25C3/06

Claims Analysis

Total Claims: 33
Claim 1
Independent Claim 162 words
In a process for the production of metals in a multicell type furnace, by the electrolysis of metal compounds dissolved in a molten electrolyte, comprising the steps of: disposing a first anode and a first cathode spaced apart therefrom in the furnace, dividing said furnace into cells by disposing at least one inconsumable bipolar electrode between said first anode and said first cathode, said bipolar electrode including a second anode the surface of which is composed of electron conductive ceramic oxide and a second cathode the surface of which is composed of another electron conductive material, joined together in such a way that, under conditions found in the operating cell, they form a mechanical and an electrical unit, maintaining a predetermined electrical potential across the first anode and the first cathode whereby a current flows through the cell and the anions have their charges removed at the anodes, and the metal ions have their charges removed at the surface of the cathodes.
Claim 2
Dependent Claim 162 words
In a process for the production of metals in a multicell type furnace, by the electrolysis of metal compounds dissolved in a molten electrolyte, comprising the steps of: disposing a first anode and a first cathode spaced apart therefrom in the furnace, dividing said furnace into cells by disposing at least one inconsumable bipolar electrode between said first anode and said first cathode, said bipolar electrode including a second anode the surface of which is composed of electron conductive ceramic oxide and a second cathode the surface of which is composed of another electron conductive material, joined together in such a way that, under conditions found in the operating cell, they form a mechanical and an electrical unit, maintaining a predetermined electrical potential across the first anode and the first cathode whereby a current flows through the cell and the anions have their charges removed at the anodes, and the metal ions have their charges removed at the surface of the cathodes.
Claim 3
Dependent Claim 22 words
In a process as claimed in claim 1, wherein said metal compound is a metal oxide, and said anions are oxygen ions.
Claim 4
Dependent Claim 20 words
In a process as claimed in claim 1, wherein said metal is aluminum and said metal oxide is aluminum oxide.
Claim 5
Dependent Claim 28 words
In a process as claimed in claim 1, wherein said second cathode is composed of materials compatible with the second anode materials under operating conditions of the cell.
Claim 6
Dependent Claim 21 words
Process in accordance with claim 1, whereby the current density at the anode surfaces is at least 0.001 A/cm 2 .
Claim 7
Dependent Claim 17 words
Process in accordance with claim 5, whereby the current density is at least 0.01 A/cm 2 .
Claim 8
Dependent Claim 17 words
Process in accordance with claim 6, whereby the current density is at least 0.025 A/cm 2 .
Claim 9
Dependent Claim 34 words
Process in accordance with claim 1, characterized in that, the surface level of the molten electrolyte is so maintained, that at least the free surface of the anode is completely immersed in the melt.
Claim 10
Dependent Claim 28 words
Method in accordance with claim 8, wherein the top surface of the electrolyte melt lies in the region of the upper edge of the frame of the electrode.
Claim 11
Dependent Claim 13 words
Method in accordance with claim 1, wherein the electrolyte has a cryolite basis.
Claim 12
Dependent Claim 13 words
Method in accordance with claim 1, wherein the electrolyte has an oxide basis.
Claim 13
Dependent Claim 131 words
In a multicell furnace for production of metals by electrolysis of metal compounds dissolved in a molten electrolyte, a first anode and a first cathode disposed spaced apart in said furnace; and at least one inconsumable bipolar electrode disposed substantially parallel to and between said first anode and first cathode dividing said furnace into separate cells, including a second anode the surface of which is composed of electron conductive ceramic oxide and a second cathode the surface of which is composed of another electron conductive material, joined together in such a way that, under conditions found in the operating cell, they form a mechanical and an electrical unit; said first and second anode being composed of the same material and said first and second cathode being composed of the same material.
Claim 14
Dependent Claim 131 words
In a multicell furnace for production of metals by electrolysis of metal compounds dissolved in a molten electrolyte, a first anode and a first cathode disposed spaced apart in said furnace; and at least one inconsumable bipolar electrode disposed substantially parallel to and between said first anode and first cathode dividing said furnace into separate cells, including a second anode the surface of which is composed of electron conductive ceramic oxide and a second cathode the surface of which is composed of another electron conductive material, joined together in such a way that, under conditions found in the operating cell, they form a mechanical and an electrical unit; said first and second anode being composed of the same material and said first and second cathode being composed of the same material.
Claim 15
Dependent Claim 23 words
Multi-cell furnace, in accordance claim 12, wherein an electrically conductive intermediate layer is arranged between anode and cathode material of the bi-polar electrode.
Claim 16
Dependent Claim 26 words
Multi-cell furnace, in accordance with claim 13, wherein the intermediate layer consists of a metal or a carbide, nitride, boride, silicide or a mixture of these.
Claim 17
Dependent Claim 17 words
Multi-cell furnace, in accordance with claim 14, wherein the metal is silver, nickel, copper, cobalt or molybdenum.
Claim 18
Dependent Claim 26 words
Multi-cell furnace, in accordance with claim 12, wherein said ceramic oxide material is tin oxide, iron oxide, chromium oxide, cobalt oxide, nickel oxide or zinc oxide.
Claim 19
Dependent Claim 20 words
Multi-cell furnace in accordance with claim 16, wherein said ceramic oxide is doped with at least one other metal oxide.
Claim 20
Dependent Claim 30 words
Multi-cell furnace in accordance with claim 17, wherein said ceramic oxide consists of SnO 2 and at least one other metal oxide in a concentration of 0.01 - 20 %.
Claim 21
Dependent Claim 22 words
Multi-cell furnace in accordance with claim 18, wherein the other metal oxide is present in a concentration of 0.05 - 2 %.
Claim 22
Dependent Claim 40 words
Multi-cell furnace in accordance with claim 17, wherein the metallic components of the additional oxide are selected from the group consisting of Fe, Sb, Cu, Mn, Nb, Zn, Cr, Co, W, Cd, Zr, Ta, In, Ni, Ca, Ba and Bi.
Claim 23
Dependent Claim 29 words
Multi-cell furnace, in accordance with claim 20, wherein said ceramic oxide is doped with 0.5 - 2 % CuO and 0.5 - 2 % Sb 2 O 3 .
Claim 24
Dependent Claim 29 words
Multi-cell furnace in accordance with claim 12, wherein the cathode of the bipolar electrode is made of carbon or borides, carbides, nitrides or silicides which are good electrical conductors.
Claim 25
Dependent Claim 16 words
Multi-cell furnace in accordance with claim 22, wherein the cathode is made of carbon as graphite.
Claim 26
Dependent Claim 55 words
Multi-cell furnace in accordance with claim 22, wherein the cathode is made of a material selected from the group consisting of borides, carbides, nitrides or silicides of the elements C and Si of the IV main group, the metals of the IV - VI subgroups of the periodic system of elements or mixtures of these.
Claim 27
Dependent Claim 22 words
Multi-cell furnace in accordance with claim 24, wherein the cathode is made of titanium carbide, titanium boride, zirconium boride or silicon carbide.
Claim 28
Dependent Claim 27 words
Multi-cell furnace in accordance with claim 16, wherein the anode or cathode or both are made as an adherent coating on a substrate using a known method.
Claim 29
Dependent Claim 15 words
Multi-cell furnace in accordance with claim 26, wherein the substrate serves as an intermediate layer.
Claim 30
Dependent Claim 37 words
Multi-cell furnace in accordance with claim 12, wherein the individual parts of the bi-polar electrode are held together by a holding means which is a poor electrical conductor and which is stable at the temperature of operation.
Claim 31
Dependent Claim 22 words
Multi-cell furnace in accordance with claim 28, wherein said holding means consists of boron nitride, silicon nitride, aluminum oxide or magnesium oxide.
Claim 32
Dependent Claim 14 words
Multi-cell furnace in accordance with claim 28, wherein said holding means is a frame.
Claim 33
Dependent Claim 33 words
Multi-cell furnace in accordance with claim 12, wherein the individual parts of the electrode are operable to be held in place by solidified electrolytic material and insulated in recesses in the furnace lining.

References Cited (Backward Citations)

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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) 1979-01-05 1979-07-07 1980-01-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-01-05 1983-07-07 1984-01-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-01-05 1987-07-07 1988-01-06 $7700.00 Window Closed / Lapsed

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