THE USE OF SODIUM BETA-ALUMINA FOR CONTROLLING THE RATE OF SODIUM ADDITION TO ALUMINUM-ALLOYS

Citation
G. Doughty et al., THE USE OF SODIUM BETA-ALUMINA FOR CONTROLLING THE RATE OF SODIUM ADDITION TO ALUMINUM-ALLOYS, Solid state ionics, 86-8, 1996, pp. 193-196
Citations number
6
Categorie Soggetti
Physics, Condensed Matter","Chemistry Physical
Journal title
ISSN journal
01672738
Volume
86-8
Year of publication
1996
Part
1
Pages
193 - 196
Database
ISI
SICI code
0167-2738(1996)86-8:<193:TUOSBF>2.0.ZU;2-P
Abstract
Sodium, when added at concentrations of 30-200 ppm, can be used to mod ify the microstructure and properties of a number of aluminium alloys. This has traditionally been achieved by physically adding a sodium ri ch alloy or flux to the melt. However, this method suffers from consid erable inefficiency since much of the sodium burns or evaporates on th e surface of the metal generating fumes and dress. A much cleaner and more efficient process is under development using a sodium ion conduct ing solid electrolyte to separate a source of sodium from the molten a luminium alloy. Under the influence of an applied potential, sodium is transported through the solid electrolyte with the rate of sodium add ition to the melt controlled by the current flow. An additional advant age of using an electrochemical sodium addition method is that it lend s itself to control via a solid state sodium sensor, This can be used to continuously measure changes in sodium activity in the alloy leadin g to improved process control. In practice, this system gives a much g reater level of control over the rate of sodium addition and because t he additions are made continuously within the molten metal, dress and fumes are virtually eliminated from the process. Experiments have been performed in laboratory, intermediate and industrial environments and this has been shown to be a viable method of controlling the sodium c ontent of aluminium alloys at industrial scales. Small portions of sol id electrolyte have been shown capable of withstanding a current densi ty in excess of 1.3 A cm(-2). A standard 200 X 30 mm electrolyte tube has been operated at a current density of approximately 0.6 A cm(-2), supplying sodium at a rate of 1.8 g min(-1) to a launder of aluminium. This rate of addition from a single tube is able to continuously supp ly the desired quantity of sodium to two tonnes per hour of aluminium alloy. Alternatively, smaller static pots of aluminium may be rapidly brought up to the desired sodium concentration and maintained at that level by adding more sodium to compensate for any evaporation.