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Circulating Particulate Bed Cathode for Metal Recovery

Research output: Contribution to conference - Without ISBN/ISSN Abstractpeer-review

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Circulating Particulate Bed Cathode for Metal Recovery. / Cheng, Chun-Yee; Dawson, Richard; Kelsall, Geoff et al.
2006. Abstract from 57th Annual Meeting of ISE, Endinburgh, United Kingdom.

Research output: Contribution to conference - Without ISBN/ISSN Abstractpeer-review

Harvard

Cheng, C-Y, Dawson, R, Kelsall, G & Robson, A 2006, 'Circulating Particulate Bed Cathode for Metal Recovery', 57th Annual Meeting of ISE, Endinburgh, United Kingdom, 31/08/06 - 5/09/06.

APA

Cheng, C-Y., Dawson, R., Kelsall, G., & Robson, A. (2006). Circulating Particulate Bed Cathode for Metal Recovery. Abstract from 57th Annual Meeting of ISE, Endinburgh, United Kingdom.

Vancouver

Cheng C-Y, Dawson R, Kelsall G, Robson A. Circulating Particulate Bed Cathode for Metal Recovery. 2006. Abstract from 57th Annual Meeting of ISE, Endinburgh, United Kingdom.

Author

Cheng, Chun-Yee ; Dawson, Richard ; Kelsall, Geoff et al. / Circulating Particulate Bed Cathode for Metal Recovery. Abstract from 57th Annual Meeting of ISE, Endinburgh, United Kingdom.1 p.

Bibtex

@conference{1efd759c73e54bdcb6cb5ac84dc7cf6b,
title = "Circulating Particulate Bed Cathode for Metal Recovery",
abstract = "Applications of electrochemical technology involving low reactant concentrations often require electrodes with high mass transport rates and specific surface areas to increase cross-sectional current densities and optimise capital and operating costs. For electrodeposition of metals from dilute solutions, cathode feeder electrodes contacting unconsolidated beds of moving, conducting particles that can grow, achieve these requirements, and enable continual harvesting of the metallic product by hydraulic transport from the bed of the particles, the relative motion of which may facilitate adherent and coherent deposit morphologies. One design option, shown schematically in Fig.1, is a circulating particulate bed electrode [1,2], for which experimental results will be reported and compared with model predictions for recovery of: 1. low concentrations of platinum from aqueous iodide solutions with simultaneous generation of tri-iodide on a carbon felt anode (Fig.1);2. metals from acidic aqueous chloride solutions, produced by the leaching of waste electrical and electronic equipment (WEEE), containing precious metals (Ag, Au, Pd) in low concentrations and base metals (Cu, Pb, Sn etc.) in high concentrations.",
author = "Chun-Yee Cheng and Richard Dawson and Geoff Kelsall and Anna Robson",
year = "2006",
month = aug,
day = "31",
language = "English",
note = "57th Annual Meeting of ISE ; Conference date: 31-08-2006 Through 05-09-2006",

}

RIS

TY - CONF

T1 - Circulating Particulate Bed Cathode for Metal Recovery

AU - Cheng, Chun-Yee

AU - Dawson, Richard

AU - Kelsall, Geoff

AU - Robson, Anna

PY - 2006/8/31

Y1 - 2006/8/31

N2 - Applications of electrochemical technology involving low reactant concentrations often require electrodes with high mass transport rates and specific surface areas to increase cross-sectional current densities and optimise capital and operating costs. For electrodeposition of metals from dilute solutions, cathode feeder electrodes contacting unconsolidated beds of moving, conducting particles that can grow, achieve these requirements, and enable continual harvesting of the metallic product by hydraulic transport from the bed of the particles, the relative motion of which may facilitate adherent and coherent deposit morphologies. One design option, shown schematically in Fig.1, is a circulating particulate bed electrode [1,2], for which experimental results will be reported and compared with model predictions for recovery of: 1. low concentrations of platinum from aqueous iodide solutions with simultaneous generation of tri-iodide on a carbon felt anode (Fig.1);2. metals from acidic aqueous chloride solutions, produced by the leaching of waste electrical and electronic equipment (WEEE), containing precious metals (Ag, Au, Pd) in low concentrations and base metals (Cu, Pb, Sn etc.) in high concentrations.

AB - Applications of electrochemical technology involving low reactant concentrations often require electrodes with high mass transport rates and specific surface areas to increase cross-sectional current densities and optimise capital and operating costs. For electrodeposition of metals from dilute solutions, cathode feeder electrodes contacting unconsolidated beds of moving, conducting particles that can grow, achieve these requirements, and enable continual harvesting of the metallic product by hydraulic transport from the bed of the particles, the relative motion of which may facilitate adherent and coherent deposit morphologies. One design option, shown schematically in Fig.1, is a circulating particulate bed electrode [1,2], for which experimental results will be reported and compared with model predictions for recovery of: 1. low concentrations of platinum from aqueous iodide solutions with simultaneous generation of tri-iodide on a carbon felt anode (Fig.1);2. metals from acidic aqueous chloride solutions, produced by the leaching of waste electrical and electronic equipment (WEEE), containing precious metals (Ag, Au, Pd) in low concentrations and base metals (Cu, Pb, Sn etc.) in high concentrations.

M3 - Abstract

T2 - 57th Annual Meeting of ISE

Y2 - 31 August 2006 through 5 September 2006

ER -