Abstract
A bench-scale electrochemical cell for plating heavy metals, such as copper from dilute wastewaters, was designed and tested. Optimization tests were performed on simulated mine-drainage water (pH 2.6, 0.1 M Na2SO4, 0.02 Ω−1 cm−1, 150 mg L−1 Cu2+) using a vertically oriented, flow-through cell containing a carbon felt cathode. Results obtained for optimized conditions of applied potential and volume flow rate demonstrated greater than 99.9% recovery of copper metal from feed solutions at an ohmic corrected potential of −0.70 V vs Ag/AgCl and flow rates approaching the design maximum of about 0.30 mL s−1. The effluent concentration of copper under conditions of optimum potential and flow rate could be routinely reduced to a target level of 50 μg L−1.
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Hatfield, T.L., Kleven, T.L. & Pierce, D.T. Electrochemical remediation of metal-bearing wastewaters Part I: Copper removal from simulated mine drainage waters. J Appl Electrochem 26, 567–574 (1996). https://doi.org/10.1007/BF00253454
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DOI: https://doi.org/10.1007/BF00253454