Liquid-solid mass transfer to a rotating mesh electrode in a rotor-stator spinning disc configuration
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Mass transfer rates of rotating meshes and flat discs in rotor–stator spinning disc reactors are presented.

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Volumetric mass transfer coefficient is 5 times higher for the mesh than for the disc.

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Virtually the same energy dissipation rates for rotating mesh and flat disc were measured.

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No increase in power consumption for the rotating mesh compared to the flat disc at equal Reynolds number.

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Results were fitted to Sherwood correlation and compared with available literature.

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