A study of natural convection in an electrochemical system with a Rayl
eigh number of the order 10(10) is presented. Theoretical and experime
ntal results for the unsteady behaviour of the concentration and veloc
ity fields during electrolysis of an aqueous solution of a metal salt
are given. The cell geometry is a vertical slot and the reaction kinet
ics is governed by a Butler-Volmer law. To reduce the effects of strat
ification, the flush mounted electrodes are located (symmetrically) in
the middle parts of the vertical walls. It is demonstrated, both theo
retically and experimentally, that a weak stratification develops afte
r a short time, regardless of cell geometry, even in the central part
of the cell. This stratification has a strong effect on the velocity f
ield, which rapidly attains boundary layer character. Measured profile
s of concentration and vertical velocity at and above the cathode are
in good agreement with numerical predictions. For a constant cell volt
age, numerical computations show that between the initial transient an
d the time when stronger stratification reaches the electrode area, th
e distribution of electric current is approximately steady.