“…Many studies have appeared on the modelling and simulation of hydrodynamical processes in electrochemical cells . Different configurations have been investigated such as stationary or rotating disk electrodes [5][6][7][8][9][10][16][17][18]23,17,[25][26][27][28][29][30][31][35][36][37], ring-disk electrodes [13,17,18] line electrodes [32], paddle cells [33,34], rotating hemispheral electrodes (RHSE) [40,41], wall-jet electrodes [44], etc. We note that usually the authors consider monodimensional flux and that bidimensional full calculations have attracted less attention, mainly in relation to electromigration phenomena during electrolysis processes [15].…”