Abstract

According to the properties of bioleaching solutions of printed circuit boards (PCBs), impurities in the leaching solution were removed by solvent extraction with N902 (2-hydroxy-5-nonylbenzaldoxime), then the purified solution was subjected to electrolyse for the production of metallic copper. The influence of equilibration time, extractant concentration, O/A ratios, pH value on copper(II) extraction and sulphuric acid concentration on copper(II) stripping had been studied. More than 97.45% of copper can be extracted from a typical bioleaching solution of PCBs after copper extraction was carried out using 10% N902 diluted in kerosene at O/A ratio of 1:1. And more than 93.57% of copper can be stripped from the loaded organic stripped at 1:1 phase ratio with 1.8 M H <sub xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink">2</sub> SO <sub xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink">4</sub> in a single stage. Copper plate with purity higher than 99.83% can be obtained after the electrowinning was conducted at a current density of 200-250 A/m <sub xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink">2</sub> at ambient temperature. Results of the present investigation indicated that bioleaching-solvent extraction-electrowinning could be a new cleaner hydrometallurgy route for recovery copper from the PCBs.

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