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P. Robertson, N. Ibl (1977)
Electrolytic recovery of metals from waste waters with the ‘Swiss-roll’ cellJournal of Applied Electrochemistry, 7
G. Kreysa (1980)
Particle phase conductivity of a fluidized bed electrodeElectrochimica Acta, 25
M. Fleischmann, J. Oldfield (1971)
Fluidised bed electrodes: Part I. Polarisation predicted by simplified modelsJournal of Electroanalytical Chemistry, 29
G. Kreysa, C. Reynvaan (1982)
Optimal design of packed bed cells for high conversionJournal of Applied Electrochemistry, 12
G. Kreysa (1978)
Kinetic behaviour of packed and fluidised bed electrodesElectrochimica Acta, 23
J. Backhurst, J. Coulson, F. Goodridge, R. Plimley, M. Fleischmann (1969)
A Preliminary Investigation of Fluidized Bed ElectrodesJournal of The Electrochemical Society, 116
K. Keating, J. Williams (1976)
The recovery of soluble copper from an industrial chemical wasteResource Recovery and Conservation, 2
J. Newman, C. Tobias (1962)
Theoretical Analysis of Current Distribution in Porous ElectrodesJournal of The Electrochemical Society, 109
A. Beenackers, W. Swaaij, A. Welmers (1977)
Mechanism of charge transfer in the discontinuous metal phase of a fluidized bed electrodeElectrochimica Acta, 22
G. Kreysa (1981)
Normalized space velocity—a new figure of merit for waste water electrolysis cellsElectrochimica Acta, 26
F. Coeuret (1980)
The fluidized bed electrode for the continuous recovery of metalsJournal of Applied Electrochemistry, 10
M. Fleischmann, J. Oldfield, L. Tennakoon (1971)
Fluidized bed electrodes Part IV. Electrodeposition of copper in a fluidized bed of copper-coated spheresJournal of Applied Electrochemistry, 1
A. Monhemius, P. Costa (1975)
Interactions of variables in the fluidised-bed electrowinning of copperHydrometallurgy, 1
G. Kreysa (1978)
Festbettelektrolyse — ein Verfahren zur Reinigung metallhaltiger AbwässerChemie Ingenieur Technik, 50
G. Kreysa, E. Heitz (1976)
Reaktions- und verfahrenstechnische Aspekte elektrochemischer Fest- und Wirbelbett-ZellenChemie Ingenieur Technik, 48
Electrochemistry with three‐dimensional electrodes. Three‐dimensional electrodes such as are used in fixed‐bed and fluidized bed electrolysis are suitable for purifying waste water containing heavy metals and for metal recovery from dilute solutions, and also open up new possibilities for electrochemical purification of waste gases. An account of the theoretical principles of the macrokinetics of these systems is followed by descriptions of a waste‐water purification process by fixed bed electrolysis, which is already in industrial use, of the rotating fixed‐bed electrode, and of the state of the art of fluidized bed electrolysis for production of metals. An electrochemical absorption tower permits removal of chlorine and sulphur dioxide from waste gases.
Chemie-Ingenieur-Technik (Cit) – Wiley
Published: Jan 1, 1983
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