A theory of anode dissolution of metals under conditions of salt passivatio
n of the surface was developed. An equation for the rate of this process as
a function of the anode potential, kinetic constants, local porosity of th
e protective layer, and other parameters was inferred. A model of functioni
ng of the protective salt layer was considered. It was demonstrated that th
e structure of this layer should be porous and fluctuating to provide for t
he access of the electrolyte to the metal surface-otherwise the surface is
screened by a continuous static layer and the anode dissolution cannot occu
r.