J. Zoric et al., MATHEMATICAL-MODELING OF ALUMINUM CELLS WITH PREBAKED ANODES .2. CURRENT DISTRIBUTION AND INFLUENCE OF SIDELEDGE, Journal of Applied Electrochemistry, 27(8), 1997, pp. 928-938
The current distribution at the electrodes in an industrial aluminium
cell with prebaked anodes was calculated. The difference between the p
rimary and secondary current distribution was determined for three dif
ferent gaps between anodes or between anode and sidewall (2.5, 10 and
30 cm). The calculated current densities at the vertical sides of the
anode were higher for the secondary current distribution than for the
primary (almost double at the uppermost part of the anode), while the
differences were much smaller at the cathode (6-20%). If the conductin
g carbon sidelining is exposed to the electrolyte it will draw an aver
age current density of 0.045 A cm(-2) for a 30 cm distance to the cath
ode. If all this current leads to the formation of aluminium carbide w
ith subsequent dissolution into the electrolyte, the sidelining will c
orrode at a rate of 0.08 cm d(-1) of exposure. The influence of the sh
ape and position of the ledge on the anode current distribution was st
udied. When the distance between the ledge and anode was greater than
15 cm the shape of the sideledge does not affect the anode current den
sities significantly, while the current density at the upper part of t
he anode increases with increasing distance.