Progress in electrochemical flow reactors for laboratory and pilot scale processing

Abstract

The principles governing the selection of an appropriate type of electrochemical flow reactor for use at laboratory or pilot scale are reviewed. Good practice in electrochemistry and electrochemical engineering must be incorporated, together with practical aspects, such as the form of reactants and products, the required performance, ease of assembly, the maintenance schedule and scale-up plans. Diverse electrode forms and reactor designs are illustrated by examples from the authors’ laboratories. The versatile parallel plate geometry, often in modular, filter-press format, occupies a prominent position, both in the laboratory and in industry. The simple parallel plate geometry is readily enhanced by inclusion of porous, 3-dimensional electrodes, structured electrode surfaces and bipolar electrical connections, with necessary consideration of the reaction environment, especially potential- and current-distributions, uniformity of flow and mass transport rates, electrode activity, side reactions and current leakage. More specialised electrode geometries, such as concentric reactors, rotating cylinder electrodes, porous electrodes, packed beds, fluidised beds and bipolar trickle towers, are sometimes chosen. Applications span materials recycling, environmental treatment and electrosynthesis. A decision tree to aid the choice of reactor design features is provided. Recent trends, such as fast prototyping of reactors via 3-D printing of flow channels, miniaturisation and use of multi-physics modelling, are highlighted. Future research and development needs are suggested.

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Identifiers

ORCID for Carlos Ponce De Leon Albarran: orcid.org/0000-0002-1907-5913

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