The ferricyanideferrocyanide redox system was studied undernaturalconvection conditions at vertical nickel electrodes by observations of the limiting current density of the cathodic process for electrodes of different heights. In the range 9 x 100 < ScGr < 4.57 x 101' the results lead to Nu = 0.45(S
Natural convection mass transfer at vertical electrodes under turbulent flow conditions
β Scribed by M.G. Fouad; N. Ibl
- Publisher
- Elsevier Science
- Year
- 1960
- Tongue
- English
- Weight
- 925 KB
- Volume
- 3
- Category
- Article
- ISSN
- 0013-4686
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β¦ Synopsis
Turbulent natural convection in electrolysis with vertical electrodes was studied by a dark field method (making the flow pattern visible) and by the method of the current/voltage curve(yielding the limiting current and the mass transfer rate). The range studied (2 x 101'< SC Gr < 1016) included the region of transition from laminar to turbulent flow. In therange 4 x lOl8 < SC Gr < lOI the results of the limiting current measurements can be represented in dimensionless form by the relation Nu = 0.31 (SC Gr)0*28, which differs only slightly from the relationship valid for laminar flow (Nu = Nusselt number, SC = Schmidt number, Gr = Grashof number). With the tallest electrodes used (which were up to 1 m high) the limiting current density tends, however, to become independent of height. From the optical experiments, as well as from a comparison with heat transfer data taken from the literature, it appears that the transition to turbulent flow is not governed solely by the product SC Gr, but depends on the value of Schmidt number too.
π SIMILAR VOLUMES
Mass transfer at horizontal plane plate electrodes under forced laminar and turbulent convection is treated for the two cases: I. Uniform potential (limiting c.d.) and II. Uniform c.d. (normal electrolysis). Expressions are derived for the thickness 6, of the diffusion boundary layer, the limiting c
NOhfENCUWRE c bulk concentration, Mcum3 d disk diameter, cm D diffusion coefficient, cm%-' IliEn0 mass transfer limiting currenr. mAcm-' 'linl., mass trausfer limitiug currenf n&m-\*, in solutions with suspended solids nF RC? SC 11 v, 2
and to indicate potential control difficulties. A similar analysis (Tung and Edgar, 1979) for a fluid catalytic cracker has also highlighted potential difficulties with single loop control. Therefore the dynamic RGA usefully augments the information provided by d static RGA. The analysis can be impl