“…In the process of non-uniform deposition of the metal inside the PE, we take into account temporal changes of the local values of filament diameters (and therefore the porosity and specific surface) as well as the linear rate of solution flow and the mass transfer coefficient of the electrically active components. For the metal deposition at a PE with low initial conductivity, we additionally took into account changes in the local conductivity of the solid phase, depending on the electric conductivity of the initial filaments and the cathode deposit [17]. All the calculations were carried out for the porous cathode with the back current feeder and back solution feed with rather high fixed solution flow rate 1 cm 3 s À1 through 1 cm 2 of the geometric area of the PE cross section.…”