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A mass-transfer study of two-phase flow in an electrochemical reactor
Authors:D. Jennings  A.T. Kuhn  J.B. Stepanek  R. Whitehead
Affiliation:1. Department of Chemistry and Applied Chemistry, University of Salford, Salford M5 4WT, Lancs, England;2. Department of Chemical Engineering, University of Salford M5 4WT, Lancs, England
Abstract:The electrodeposition of Cu2+ ions from a solution of 1 M H2SO4 has been studied in a parallel plate cell with two-phase (liquidgas) flow. The results are interpreted in terms of the LevichLandau and TaylorPrandtl models. The conclusion is reached that the mass-transfer enhancement observed results mainly from increase in linear velocity of the liquid phase due to a reduction of the effective cross-sectional area of the cell caused by the bubbles. The industrial prospects for such a system are discussed.
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