LEDGE-FREE ALUMINIUM SMELTING CELL

Abstract: An aluminium smelting cell comprising side walls (5) and a floor (2) defining an active cathode, an anode (3) overlying the cathode floor (2), some said side walls (5) being covered by a wetted cathode material (6), such as one contained TiB2, so that the covered side walls become active cathode surfaces on which a film of aluminium metal forms to protect the side wall parts against bath attack, thereby enabling the cell to operate at the desired temperatures without the usual protective side ledge of the frozen electrolyte material.

Description: TTTT.F.. τ.wnι_ -_ ALUMINIUM SMELTING CELL Field of the Invention . This invention relates to improvements in aluminium smelting cells, and more particularly relates to an aluminium smelting cell which is capable of operation without the usual protective side ledge of frozen electrolyte material. Background of the Invention: The technical and patent literature relating to the construction and operation of aluminium smelting cells invariably supports the firmly entrenched belief that an aluminium smelting cell must operate with a stable ledge of frozen electrolyte material protecting the regions of the side wall of the cell contacted by thf lectrolyte bath and the molten aluminium produced the _by against the destructive action of the electrolyte and aluminium melts. For example in "Light ϊetals" 1979, Pages 75 to 2, Peacey & Medlin, describe the desirability of parameters of cell side wall design t ich promote the formation of a good ledge, while in "Light Metals" 1983, Pages l5 to 7, various authors, describe the factors necessary for the maintenance of a stable side ledge structure. In the patent literature, the desirability of promoting an adequate side ledge is described in many prior art patents. For example, in U.S. Patent 4,608,135 Brown uses artificial cooling of the side wall to induce the formation of an adequate side edge, while in U.S. Patent 4,466,995 Boxall et al, describes a cell structure which controls the size of the side wall ledge but nevertheless indicates that the formation of such a ledge is essential. Notwithstanding the widely recognized need for an adequate ledge in the operation of known aluminium smelting cells, the advantages of operating a cell without a ledge are well understood but have not thus far been able to be achieved other than by substantial reductions in cell operating temperatures coupled with substantial modifications to the bath chemistry (set U.S. Patent 5,006,209, Beck et al). Summary of Invention said Objects: It is the object of the present invention to provide modifications to the aluminium smelting cell structure which enable operation of the cell without a ledge while being able, if desired, to maintain standard operating temperatures and bath chemistries. The invention provides an aluminium smelting cell comprising side walls and a floor defining an active cathode, at least one anode in overlying relationship with said cathode floor, characterized in that at least a part of each side wall of said cell is covered by means of a wetted cathode material, the or each anode having portions which are adjacent said covered parts of said side walls whereby said side wall parts become active cathode surfaces of the cell on which a film of aluminium metal will form to protect the side wall parts against erosion. In a preferred form of the invention, the side walls of the aluminium smelting cell should be covered by said wetted cathode material to a height at least corresponding to the expected height of the cell bath. In this way, the need for the establishment of a protective ledge in the cell may be substantially avoided whereby the heat balance of the cell can be more easily controlled. The elimination of the frozen side ledge means that there is an increased volume of molten bath available for dissolution of alumina. This helps to decrease the risks of anode effects which, in turn, reduces the related voltage, thermal imbalance and cell control penalties. The shape of the side ledge influences the shape of the cell metal pad reservoir (in the case of an undrained cathode cell) through the altered current pathways caused by its insulating presence. The elimination of the ledge leads to a more predictable and consistent current distribution and therefore metal pad profile, which in turn allows a more precise anode to SUBSTITUTE HEE - 3 - cathode distance to be set and controlled. The voltage benefit to be gained by a lower cu . density cell operation requires a more heavily insulated cell to compensate for the lower heat generation. These benefits would be severely restricted, or unobtainable, if it were also necessary to maintain a frozen side ledge through under-insulation or forced cooling of the side wall. Brief Description of the Drawings: In order that this invention may be more readily understood, a preferred embodiment of the invention will now be described with reference to the accompanying drawings in which: Figure 1 is a schematic sectional end elevation of an aluminium smelting cell embodying the present invention; Figure 2 illustrates an example of the location of the liquidus point isotherm in a drained cathode cell embodying the present invention; Figure 3 illustrates the 5% current distribution lines of a standard aluminium smelting cell operating with a side wall of frozen electrolyte; Figure 4 is an illustration similar to F_ re 4 showing the 5% current distribution lines for a cell embodying the present invention, and Figure 5 is a schematic sectional end elevation of an alternative cell configuration embodying the present invention; Description of the Preferred Embodiment: Referring firstly to Figure 1 of the drawings, the a^iminium smelting cell 1 embodying the invention is & wn schematically +-0 include floor portio 1 -: 2 defining an active cathode, an anoά having an a 3 surface 4 overlying the cathode 2, nd a side w<_ ._ 5 extending angularly and upwardly from the floor portion 2 in the manner generally shown in Figure 1. In the present embodiment, the floor portion 2 and the side wall 5 are covered _y means of a wetted cathode material 6, such as a TiB 2 containing compound known in the art. The wetted cathode material 6 is shown as extending to the top of the side wall 5, although in practice it is only necessary for the material to extend to a height equal to or slightly above the height at which the molten bath 7 of the cell is known to extend. In the embodiment shown, the cell is of horizontal drain construction having a central sump 8 for collecting the molten metal from the surface of the cathode 6. However, the covering of the side wall 5 with a wetted cathode material may be applied to any cell construction to provide the advantages of ledge-free operation. It will be appreciated that by covering the lower side wall fillet or ram and the upper side wall portion with a wetted cathode material, and keeping them ledge- free, these surfaces form part of the active cathode surface on which a film of aluminium metal will form. This results in the following advantageous cell features: (1) Depending on the proximity of the anode, the near side edge of the anode can be induced to burn to the desired profile to facilitate the controlled release of bubbles described earlier, as well as encouraging sufficient induced bath flow along the length of the anode to yield a good alumina supply into the ACD. (ii) The active metal-covered sidewall is thus made more resistant to bath attack and the need for maintaining a protective sidewall ledge is removed. Ledgeless cell operation reduces the need for very stringent heat balance controls, increases the available bath volume in the cell and provides increased control flexibility. Figure 2 of the drawings shows that by appropriate cell design and use of insulation the liquidus point isotherm I in a cell embodying the present invention lies outside the active region of the cell and intersects the side wall 5 a the point of intersection of the side wall and the crust 9 which forms over the SUBSTITUTESHEE bath in operation. Figures 3 and 4 of the drawings illustrate the 5% current distribution lines in a standard cell (Fig. 3) and in a cell embodying the present invention (Fig. 4). In Figure 3, the frozen side ledge which traditionally forms is illustrated at 10. It will be noted that the anode 3 substantially retains its original essentially rectangular configuration at the edges and there is little anode profiling of the type referred to above. This leads to an increase in the bubble layer resistance beneath the anode thus increasing the operating voltage of the cell. Figure 4 of the drawings clearly shows that the wetted cathode material covered side wall 5 is active and will therefore be covered by a thin film of molten aluminium which in turn protects the side wall against bath attack. The current densities in the regions A to D shown in Figure 4 were found to be of the order of 0.2 A/cm 2 , while the current density in the main cathode region was of the order of 0.7 A/cm 2 . At the above relative cathode current densities, metal should be deposited on the surface of the side wall 5 at approximate! one-quarter of the rate of metal production on the bulk cathode. Further molten metal may be provided by surface tension driven flow of metal from the cathode region up the side wall. Accorα_.ngly the current passing through the side wall 5 is sufficient to generate the formation of an aluminium metal film covering the side wall to provide protection from attack by the molten electrolyte 7. Furthermore, since the sue wall 5 is active, the anode 3 is profiled as shown in Figure 4 to provide for controlled release of bubbles from beneath the anode 3 which lowers the bubble layer resistance beneath the anode 3 and consequently reduces the operating voltage of the cell. In order to achieve ledge-free operation in the side wall regions, additional insulation will be required in the side wall structure and the super heat of the cell will increase to probably greater than 20°C. High energy efficiency can be achieved whilst operating at high bath super heat and these conditions also promote good alumina dissolution which minimizes sludge formation. This may enable the cell electrolyte to be significantly modified so that electrolytes with very much lower melting (and therefore operating) point temperatures may be used, for example, from 50°C to about 850°C. Such a reduction in cell electrolyte temperature will reduce the cell heat loss by approximately 10 and should thereby increase the energy efficiency by about \W. . Ledge-free cell operation will also result in an increased electrolyte volume which will permit enhanced alumina dissolution and thereby result in smaller alumina concentration swings between alumina additions. It will be appreciated from the above that the elimination of the frozen side wall ledge provides for greater latitude, flexibility and simplicity in cell operation. The substantial heat extraction required to form the frozen side ledge results in thermally inefficient cell operation, and the absence of the need for a ledge significantly improves thermal efficiency. Similarly, the present of a side ledge constrains the temperature of the electrolyte to values very close to its liquidus point, usually about 5 to 10°C above it. This low level of super heat imposes restrictions on the dissolution of alumina in the bath and the consequential formation of sludge. As mentioned above, elimination of the side ledge allows larger super heat values to be employed and this provides a corresponding benefit in alumina dissolution capability and reduction in sludge formation. Furthermore, since the frozen side ledge is usually pure cryolite, whilst the molten electrolyte is a closely controlled mixture of components, the dynamic freezing and remelting of the side ledge leads to variations in the bath composition and difficulties in maintaining stable bath composition. The absence of the side ledge will provide consequential improvements in the stability of bath composition. SUBSTITUTE In the modified cell design of Figure 5 of the drawings, the lower side wall fillet or ram is supplemented by an abutment or protrusion 10 formed on the surface of the cathode 2 adjacent the side wall 5- The abutment is preferably covered by means of a wetted cathode material similar to the material 6 which covers the side wall 5 and the cathode 2 and operates to cause specific profiling of the edge of the anode 3, in the manner illustrated in Figure , as well as inducing bath flow to ensure a good supply of alumina-enriched bath into the electrolysis zone. In all other respects, the operation of this embodiment is similar to the operation of the embodiment of Figure 1. The cell designs des< ribed above may be modified to suit any given set of circumstances and may incorporate any one of the design features described in greater detail in our co-pending Patent Application of even date herewith entitled "Improved Aluminium S* ^lting Cell", which claims priority from Australian Patent Application No. PK 1843 dated 20th August 19 r ^. Similarly, the cell may incorporate any one of the design features described in greater detail in our co-pending Patent Application No. Au-A 50008/90 or in corresponding United States Serial No. 07/481847 Stedman et al.

Claims: Claims 1. An aluminium smelting cell comprising side walls and a floor defining an active cathode, at least one anode in overlying relationship with said cathode floor, characterized in that at least a part of each side wall of said cell is covered by means of a wetted cathode material, the or each anode having portions which are adjacent said covered parts of said side walls whereby said side wall parts become active cathode surfaces of the cell on which a film of aluminium metal will form to protect the side wall parts against bath attack. 2. The cell of claim 1, wherein said wetted cathode material covers said side wall to a level which at least corresponds to the intended level of the electrolyte bath within the cell. 3. The cell of claim 2, wherein the cathode is similarly covered with said wetted cathode material. 4. The cell of any preceding claim, wherein said side wall extends outwardly and upwardly from said cathode to cause profiling of the edge of said anode to encourage controlled bubble release and electrolyte flow.. 5. The cell of any one of claims 1 to 3, further comprising an abutment or a protrusion formed on the cathode adjacent the side wall and shaped to cause profiling of the edge of said anode to encourage controlled bubble release and electrolyte flow. 6. A method of operating an aluminium smelting cell having side walls, a cathode floor and at least one anode in overlying relationship with said cathode floor, comprising covering at least part of the side walls with a wetted cathode material, operating the cell whereby the covered side wall parts become active cathode surfaces on which a film of aluminium metal forms to protect the side wall parts against bath attack. SUBSTITUTESHEE

Inventors: COAD IAN A, HOUSTON GEOFFREY J, JURIC DRAGO D, SHAW RAYMOND W, COAD, IAN, A., HOUSTON, GEOFFREY, J., JURIC, DRAGO, D., SHAW, RAYMOND, W.
Applicants: COMALCO ALU, COMALCO ALUMINIUM LIMITED
Application year: 1991
Main classification: C25C3
IPC codes: C25C3