In 2014, the European Union defined a list of 20 raw materials critical for economic importance and high supply risk. The aim of this work is to present the main results achieved within the EU-FP7 Project HydroWEEE-Demo dealing with the recovery of indium and cobalt, metals included in such European list, from LCD scraps and end of life Li-ion batteries, respectively. A complete indium recovery was achieved carrying out an acidic leaching, followed by a zinc cementation. Cobalt was extracted from the electrodic powder according to the following main operations: leaching (by acid reducing conditions), primary purification (by precipitation of metal impurities), solvent extraction with D2EPHA (for the removal of metal impurities), solvent extraction with Cyanex 272 (for the separation of cobalt from nickel), cobalt recovery (by precipitation as cobalt hydroxide). Co products with 95% purity were obtained by implementation of the solvent extraction with D2EHPA and Cyanex 272
Recovery of critical metals from LCDs and Li-ion batteries / Amato, Alessia; Rocchetti, Laura; Fonti, Viviana; Atia, Thomas Abo; Altimari, Pietro; Moscardini, Emanuela; Toro, Luigi; Pagnanelli, Francesca; Beolchini, Francesca. - ELETTRONICO. - (2016), pp. 1-5. (Intervento presentato al convegno 2016 Electronics Goes Green 2016+, EGG 2016 tenutosi a Berlino nel 2016) [10.1109/EGG.2016.7829832].
Recovery of critical metals from LCDs and Li-ion batteries
ALTIMARI, PIETRO;MOSCARDINI, Emanuela;TORO, Luigi;PAGNANELLI, Francesca;BEOLCHINI, FRANCESCA
2016
Abstract
In 2014, the European Union defined a list of 20 raw materials critical for economic importance and high supply risk. The aim of this work is to present the main results achieved within the EU-FP7 Project HydroWEEE-Demo dealing with the recovery of indium and cobalt, metals included in such European list, from LCD scraps and end of life Li-ion batteries, respectively. A complete indium recovery was achieved carrying out an acidic leaching, followed by a zinc cementation. Cobalt was extracted from the electrodic powder according to the following main operations: leaching (by acid reducing conditions), primary purification (by precipitation of metal impurities), solvent extraction with D2EPHA (for the removal of metal impurities), solvent extraction with Cyanex 272 (for the separation of cobalt from nickel), cobalt recovery (by precipitation as cobalt hydroxide). Co products with 95% purity were obtained by implementation of the solvent extraction with D2EHPA and Cyanex 272File | Dimensione | Formato | |
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