Process for producing aluminum
AssigneeAluminum Company of America
InventorsRobert W. Graham, Stanley C. Jacobs, Henry G. Wickes, Jr., Alfred F. LaCamera
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Abstract
In a process for producing aluminum, which process conventionally includes electrolytically decomposing alumina to aluminum metal in a molten electrolyte bath between a carbon anode and a cathodic interface formed between a molten aluminum metal pad and sides electrolyte bath, the bath A. being predominantly NaF and AlF.sub.3, b. containing CaF.sub.2 and Al.sub.2 O.sub.3, and C. being covered by a frozen crust, The improvement including providing in the bath 5 to 10 weight-% LiF, while maintaining in the bath a weight ratio NaF to AlF.sub.3 of 1.04 to 1.15, and while maintaining a frozen layer bounding the sizes of the aluminum metal pad and bath.
Claims9
In a process for producing aluminum, which process conventionally includes electrolytically decomposing alumina to aluminum metal in a molten electrolyte bath between a carbon anode and a cathodic interface formed between a molten aluminum metal pad and the electrolyte bath, the bath
- a. being predominantly NaF and AlF.sub.3,
- b. containing CaF.sub.2 and Al.sub.2 O.sub.3, and
- c. being covered by a crust,
- the improvement comprising providing in the bath 5 to 10 weight-% LiF, while maintaining in the bath a weight ratio NaF to AlF.sub.3 of 1.04 to 1.15, and while maintaining a frozen layer bounding the sides of the aluminum metal pad and bath, with the bath temperature during electrolytic decomposition being less than 940.degree. C.
In a process for producing aluminum, which process conventionally includes electrolytically decomposing alumina to aluminum metal in a molten electrolyte bath of a side-fed cell between a carbon anode and a cathodic interface formed between a molten aluminum metal pad and the electrolyte bath, the bath
- a. being predominantly NaF and AlF.sub.3,
- b. containing CaF.sub.2 and Al.sub.2 O.sub.3, and
- c. being covered by a crust,
- the improvement comprising providing in the bath 5 to 10 weight-% LiF, while maintaining in the bath a weight ratio NaF to AlF.sub.3 of 1.04 to 1.15, and while maintaining a frozen layer bounding the sides of the aluminum metal pad and bath, with the bath temperature during electrolytic decomposition being less than 940.degree. C.
Dependencies are inferred from the claim text.