Abstract
Wastewater of a silver processing plant at the Eti Gumus plant located at Kutahya, Turkey was treated with an acidification, volatilisation and reneutralisation (AVR) process for cyanide recovery as a preliminary treatment, and with ozone and ozone/UV light plus catalysts as a secondary treatment. Average NaCN concentrations of slurry with AVR were reduced from 900 ± 50 ppm to 50 ± 10 ppm. Then, oxidation of cyanide in the presence of titanium dioxide, zinc sulphate and copper sulphate as catalysts was investigated and variations in CN− and CNO− ion concentrations were measured with a cyanide electrode and ion chromatography, respectively. The reaction time reduced to 12 min with the addition of catalysts when ozone consumption was 0·100 g min−1 after 25 min with ozone alone and 0·071 g min−1 after 20 min for the ozone/UV system. As a result, the most effective method to achieve appropriate discharge values for cyanide with respect to environmental protection laws was the ozone/UV/TiO2 system with AVR recovery for the effluents of silver ore leaching.
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