Inconsumable electrodes
AssigneeSwiss Aluminium Ltd.
InventorHanspeter Alder
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AssigneeSwiss Aluminium Ltd.
InventorHanspeter Alder
Estimating the term…
Process for operating a cell for the electrolysis of a molten charge, in particular aluminum oxide, with one or more anodes the working surfaces of which are of ceramic oxide material, and anode for carrying out the process. In the process a current density above a minimum value is maintained over the whole anode surface which comes into contact with the molten electrolyte. An anode for carrying out the process is provided at least in the region of the interface between electrolyte and surrounding atmosphere, the three phase zone, with a protective ring of electrically insulating material which is resistant to attack by the electrolyte. The anode may be fitted with a current distributor for attaining a better current distribution.
In an inconsumable anode comprising an electrode composed of ceramic oxide material, for use in electrolytic recovery of aluminum from a molten charge electrolyte containing aluminum oxide during which electrolytic recovery a predetermined minimum current density is maintained over that portion of the surface of the electrode in contact with the electrolyte to retard the reaction between the electrode and the electrolyte,
In an anode, as claimed in claim 13, wherein said current distributor consists of a metal or an electrically conductor carbide, nitride or boride.
An inconsumable anode, for use in connection with a molten electrolyte containing aluminum oxide,
Dependencies are inferred from the claim text.
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From the US filing history. Foreign family members aren’t listed.
Term ended 8 Nov 1994 (estimated)
USPTO file history isn’t available for this patent, so only indexed dates are shown.
The invention relates to a process and a device for the electrolysis of a molten charge using inconsumable electrodes, in particular for the production of aluminum with a purity of more than 99.5 %.
In the electrolytic production of aluminum by the Hall-Heroult process a cryolite melt with Al.sub.2l O.sub.3 dissolved in it is electrolysed at 940.degree. - 1000.degree. C. The aluminum which separates out in the process collects on the cathodic carbon floor of the electrolysis cell whilst CO.sub.2 and to a small extent CO are formed at the carbon anode. The anode is thereby burnt away.
For the reaction
The figures show:
FIG. 1. A ceramic oxide anode with sides completely shielded
FIG. 2 A ceramic oxide anode with sides partly shielded by solidified electrolytic material.
In all figures the part leading the power to the anode is indicated by the number 1. It is made of metal or another electron conductive material such as a carbide, nitride or boride. The protective layer 2 on the anode 3 is made of a poorly conducting material which is resistant to attack by the molten electrolyte. The ceramic oxide anode 3 consists, advantageously, of doped SnO.sub.2 and is at least partly in contact with the electrolyte 4.
In the embodiment shown in FIG. 1, the protective layer 2 on the cylindrically shaped anode 3 of ceramic oxide material, is a ring of electrically melted A1.sub.2 O.sub.3 or MgO which has been prefabricated and bonded, or sprayed onto the anode surface before immersing the anode in the melt. This protective ring completely covers the sidewalls of the ceramic anode 3 which is only partly immersed in the molten electrolyte 4. In this way a mainly uniform distribution of current is obtained on the exposed bottom face which is immersed in the molten electrolyte.
It is however not necessary that the protective ring covers the whole of the side wall area, it may also be less extensive but must protect that part in the three phase zone.