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Enhanced mass transfer at the rotating cylinder electrode: III. Pilot and production plant experience
Authors:D. R. Gabe  F. C. Walsh
Affiliation:(1) Department of Materials Engineering and Design, The University of Technology, LE11 3TU Loughborough, Leicester, UK;(2) Present address: Department of Pure and Applied Chemistry, University of Strathclyde, 295 Cathedral Street, G1 1XL Glasgow, UK
Abstract:Enhanced mass transfer at a rotating cylinder electrode, due to the development of surface roughness of a metal deposit, has been studied in a range of commercial and pilot scale reactors known as ECO-CELLS. The data obtained for relatively restricted ranges of process parameters show reasonable agreement with the more definitive data obtained under laboratory conditions. With scale-up factors of approximately six times in terms of the rotating cylinder diameter, enhanced mass transfer factors of up to 30 times are reported (in comparison with hydrodynamically smooth electrodes) due to the development of roughened deposits during the process of metal extraction from aqueous solution.Nomenclature a, b, c constants in Equation 15 - A active area of rotating cylinder (cm2) - C (bulk) concentration of metal (mol cm–3 or mg dm–3) - Deltac concentration change over reactor (mol cm–3 or mg dm–3) - CIN,COUT,CCELL inlet, outlet and reactor concentrations of metal (mol cm–3 or mgdm–3) - d diameter of rotating cylinder (cm) - D diffusion coefficient (cm2 s–1) - fR fractional conversion - F Faraday constant=96 500 A s (mo1–1) - I current (A) - IL limiting current (A) - Io useful current (A) - jD' mass transport factor (=St Scc) - K constant in Equation 27 - KL mass transport coefficient (cm s–1) - m slope of Fig. 8 (s–1) - M molar mass of copper = 63.54 g mol–1 - n number of elements in the cascade - N volumetric flow rate (cm3–1) - P Reynolds number exponent for powder formation (Equation 28) - R total cell resistance (Q) - t time (s) - U peripheral velocity of cylinder (cm s–1) - Vcell cell voltage (V) - VR,VT effective cell, reservoir volume (cm3) - W electrolytic power consumption (W) - x velocity index in Equation 27 - z number of electrons - Re Reynolds number=Ud/v - Sc Schmidt number=v/D - St Stanton number=KL/U - gu kinematic viscosity (cm2 s–1) - phgr cathode current efficiency - ohgr rotational speed (revolutions min–1) - epsiv peak to valley roughness (cm)
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