Abstract
The earlier developed dynamic model of a flow-through electrode is used for studying how the variations in initial conductivity of a porous matrix κs,ini and a metal deposit affect the rate of metal deposition from an oxidant-containing solution for the direct-flow operation mode of the porous electrode. It is found that in contrast to an oxidant-free solution in which the decrease of κs,ini improves the uniformity of deposit distribution inside the porous cathode and increases the deposit final mass mf, the opposite situation is observed in the presence of an oxidant, namely, a decrease in κs,ini, under otherwise similar conditions reduces the deposit mass and leads to its specific spatial distribution. The final metal deposit is divided into two separate fragments (rear and front) with a region of low conductivity of the initial porous matrix in between. Dynamics of the current and metal redistribution within the porous electrode, the reasons for the formation and stabilization of the rear fragment of coating, the correlation between the metal deposition rate and changes in the anodic zone position and intensity are discussed. It is shown that with the appearance of a specific profile of deposit distribution, the dependence of mf on the metal conductivity develops a limit that differs considerably from the deposit final mass for an equipotential porous electrode.
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