The mathematical treatment of mass transport in tubular electrodes has
been examined for the EC process when a reversible electrode charge t
ransfer is followed by a reversible chemical reaction. The transition
from fast chemical reaction to slow chemical reaction is investigated.
The system of convective-diffusion equations, representing the physic
al phenomena, are solved using properties of the integral transform an
d numerical computation of the integral equation. The effects of the c
hemical equilibrium parameter, the axial velocity of the flow and the
potential scan rate on theoretical current-potential curves are elucid
ated and a simple procedure to determine the chemical reaction rate co
nstant is presented.