Electrochemical
reactors with a flat parallel plate electrode configuration
and diverse flow channel designs have been extensively used in the
study of different electrochemical processes at lab and bench scales,
and they have been scaled up for some electrosynthesis and energy-storage
processes at semipilot and industrial levels. Progress in the electrochemical
process applications demands the use of different computer and experimental-assisted
techniques to design novel electrochemical reactors. The objective
of this work is to evaluate the hydrodynamic performance of different
electrochemical reactor designs and quantify their effect on velocity
magnitude through numerical and experimental studies using computational
techniques like computational fluid dynamics (CFD) and digital image
treatment. For local velocity magnitude measurements, a digital imaging
treatment, based on the use of an optical flow algorithm, to try the
validation of velocity profiles obtained by CFD is implemented. This
experimental technique determined reliably that the problems associated
with the use of the empty channel in the flow pattern are mainly associated
with high velocities and recirculation zones, which are not detected
by CFD simulations in the first instance. Also, the findings associated
with the velocity behavior using this proposed technique agreed with
those obtained by the traditional experimental flow characterization
technique like residence time distribution, nevertheless, further
work will be needed to refine the measurements and perform its comparison
with other most employed velocimetry techniques.