Correlation are presented for the rate of mass transfer to a contmuouv moving surface of a sheet electrode at nonzero veloattes of the electrolyte bulk The equations derwed are vahd for lammar flow, where the velocity of the movmg electrode surface Us and the veloctty of the bulk phase U, have the s
Mass transfer to a moving continuous cylinder
β Scribed by J.W. Rotte; G.L.J. Tummers; J.L. Dekker
- Publisher
- Elsevier Science
- Year
- 1969
- Tongue
- English
- Weight
- 482 KB
- Volume
- 24
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
A well-known electrochemical technique has been used in order to measure average mass transfer coefficients between a stagnant liquid and a moving continuous cylinder (e.g. a fibre). These experiments confirmed the theory, which has been presented in a previous paper: ShH = Cd(P&) 4.103 < d(P&) < 4.104 SC > 700. The proportionality factor, C, is a function of the Schmidt number and of the ratio of the boundary layer thickness to the wire radius (see Fig. 7). For low values of this ratio and for high Schmidt numbers, the results of both theory and experiment give C = l-13.
π SIMILAR VOLUMES
When a contmuous cylmder IS cooled by passmg lt longltudmally through a qmet flmd (free convecfion IS not consldered) then the followmg relatlon for the local heat transfer coefficlent can be glven The group d(PΓ©,)/P&. allows for the curvature of the cylmder. the fourth dlmenslonless group accommoda
Mass transfer coefficient data are presented for the transfer of solutes between isolated drops and continuous phase in a droplet file column. Radioactivity labelled, i.e. tritiated water was used as a tracer to obtain values of the individual phase coefficients in saturated binary systems. Those fo
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