Journal
JOURNAL OF CLEANER PRODUCTION
Volume 330, Issue -, Pages -Publisher
ELSEVIER SCI LTD
DOI: 10.1016/j.jclepro.2021.129879
Keywords
Plating wastewater; Pilot-scale plant; Electrodialysis; Electrowinning; Chemical precipitation
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Funding
- Konkuk University
- Korea Environment Industry & Technology Institute (KEITI) through Subsurface Environmental Management (SEM) Project - Korea Ministry of Environment (MOE) [2020002480006]
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In this study, a pilot-scale electrodialysis system was developed for the treatment of plating wastewater, concentrating metal species for selective recovery via electrowinning and chemical precipitation processes. Electrodialysis showed potential for addressing challenges in metal recovery from low concentration wastewater, demonstrating selective recovery of copper and other metals.
Metal recovery from industrial wastewater can be achieved by electrowinning (EW) and chemical precipitation (CP), but this is challenging because of the low concentration of metal ions in the wastewater, especially that from metal plating plants, as well as the presence of other organic and anionic species. However, electrodialysis (ED) is a promising method for concentrating the metal species in wastewater. Therefore, in this study, we developed and operated a pilot-scale ED system for the treatment of real plating wastewater, obtaining EDconcentrated plating wastewater in the concentration compartment for the selective recovery of Cu and other metals using pilot-scale EW and CP processes, respectively. The ED process was run at 200 V (13.3 V/cell-pair) and produced plating wastewater having metal concentrations up to two orders of magnitude greater than that of the input wastewater. A cell voltage of 2.0 V was selected for EW because it yielded an appropriate current density and the selective recovery of Cu as Cu(0) and Cu2O without producing metallic sludge. We obtained almost 93%-96% Cu-selective recovery (initial [Cu] = 790-1145 mg/L) from the ED-concentrated plating wastewater samples via our pilot-scale EW process, which had a specific energy consumption of 3.5-5.3 kWh/ kgCu. In the CP process, we found that hydroxide precipitation allowed the selective recovery of amorphous Fe (OH)3/Fe-Cr complexes at pH 4-5 and beta-Ni(OH)2/lambda-Zn(OH)2 at pH values exceeding 7. Thus, the sequential EW/ CP system is suitable for the treatment of ED-concentrated plating wastewater and the recovery of valuable metals.
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