The steady-state mass balance for dissolved oxygen in a divided rotati
ng cylinder electrode reactor was established. Cases involving the abs
ence or presence of hydrogen evolution, as in, respectively, copper an
d zinc deposition, were treated. The results show that the importance
of the diffusion controlled oxygen reduction reaction on metal deposit
ion current efficiency is considerably decreased at low electrolyte fl
ow rates used industrially by separating the reactor with a membrane,
thus preventing the oxygen formed at the anode from reaching the catho
de. Further substantial gains are achieved if hydrogen evolution takes
place in the reactor, allowing a very efficient desorption mechanism
of dissolved oxygen, but the global effect on metal deposition current
efficiency remains unfavorable. The influence of several parameters o
n dissolved oxygen concentration inside the reactor and metal depositi
on current efficiency, such as electrolyte how rate, mass transfer coe
fficient, current density and inlet electrolyte dissolved gases concen
tration (oxygen and hydrogen), is also discussed. Comparison with expe
rimental data for copper and cadmium deposition show that the derived
equations appear adequate, although more data is required to make a co
mplete assessment. Finally, the derived equations allow optimization o
f the rotating cylinder electrode reactor.