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Mass transfer at rotating cone electrodes
Authors:A F S Afshar  D R Gabe  B Sewell
Affiliation:(1) IPTME, Loughborough University of Technology, LE11 3TU Loughborough, UK;(2) Twickenham Plating Group PLC, Colne Rd., TW1 4JR Twickenham, Middlesex, UK;(3) Present address: S. G. Owen Co. Ltd., Lodge Farm Industrial Estate, NN5 7UF Northampton, UK
Abstract:Upright and inverted rotating cone electrodes (apex half angle 52°) have been studied using electrodeposition of copper from an acid electrolyte (Sc=1770) by means of limiting current mass transport techniques. The behaviour suggests that it is appropriate to regard these electrodes as modified disc electrodes. The upright rotating cone electrode exhibits a flow transition atRe=1×105. In laminar flowSh=4.5Re 0.48 and in turbulent flowSh=0.04Re 0.95. The inverted rotating cone electrode exhibits a flow transition atRe=6×104. In laminar flowSh=4.5Re 0.45 and in turbulent flowSh=0.04Re 0.88. The data have been interpreted in terms of a coating thickness affected by throwing power effects and the use of a conical cathode cell for control of high speed electrodeposition processes is indicated.Nomenclature A electrode area (cm2) - C b concentration (of bulk solution) (mol cm–3) - Deltac concentration difference (mol cm–3) - D diffusion coefficient (cm2 s–1) - f/2 friction factor - F Faraday's constant (96485 A s mol–1) - i L limiting current density (A cm–2) - J mass transfer flux (mol s–1 cm–2) - K L mass transfer coefficient (cm s–1) - l slant height of the cone (cm) - U peripheral velocity (cm s–1) - x local condition coordinate (cm) - z no. of electrons - agr apex half-angle of cone - ohgr angular velocity (rad s–1) - tau wall shear stress (dyn cm–2) - ngr kinematic viscosity (cm2 s–1) - Re Reynolds number=Ud/v - Sc Schmidt number=v/D - Sh Sherwood number=K L d/D
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