Abstract:A model for the operation of a working photoelectrochemical reactor has been developed and implemented, using the COMSOL Multiphysics TM modeling package. The model incorporates the detailed design of the practical reactor developed to use a 0.01 m 2 Fe 2 O 3 photoelectrode. Initial modeling was used to analyze electrolyte flow within the reactor and recommend modifications to the reactor design. Results indicate that improvements to flow uniformity could be achieved with some minor internal changes. Modeling … Show more
“…19 However, hitherto a model had yet to be developed for photo-electrochemical reactors, in which the photo-absorber and electrode are the same material, coupled with bubble generation at the electrode and the bulk of the electrolyte. Incorporating bubble formation at the photo-electrode|electrolyte interface is important as (i) it enables quantication of the amount of gas produced near the surface and the actual dissolved gas ux diffused into the bulk of the electrolyte that could take part in cross-over losses; 20 (ii) rates of generation of bubbles in photoelectrochemical reactors should be minimised by judicious design, to minimise resistive losses 21,22 and the reection and scattering of incoming light 23 that otherwise would decrease photo-electro-active areas. The latter effect will be addressed in more detail in a subsequent paper.…”
A photo-electrochemical cell model was developed accounting for photon flux, electron–hole recombination rates, gas desorption, bubble formation and cross-over losses.
“…19 However, hitherto a model had yet to be developed for photo-electrochemical reactors, in which the photo-absorber and electrode are the same material, coupled with bubble generation at the electrode and the bulk of the electrolyte. Incorporating bubble formation at the photo-electrode|electrolyte interface is important as (i) it enables quantication of the amount of gas produced near the surface and the actual dissolved gas ux diffused into the bulk of the electrolyte that could take part in cross-over losses; 20 (ii) rates of generation of bubbles in photoelectrochemical reactors should be minimised by judicious design, to minimise resistive losses 21,22 and the reection and scattering of incoming light 23 that otherwise would decrease photo-electro-active areas. The latter effect will be addressed in more detail in a subsequent paper.…”
A photo-electrochemical cell model was developed accounting for photon flux, electron–hole recombination rates, gas desorption, bubble formation and cross-over losses.
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