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Application of the reagentless dual-temperature ion-exchange technique to a selective separation and concentration of copper versus aluminum from acidic mine waters
Acidic mine waters represent natural effluents from pyritic ore deposits and they are mainly characterized by a low pH and a high concentration of metal ions such as Fe 3+, Zn 2+, Cu 2+, Mn 2+, A1 3+, Ca 2+, Mg 2+ and Na +. The treatment of these waters is of great economic and ecological importance...
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Published in: | Hydrometallurgy 1997-03, Vol.44 (3), p.331-346 |
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Main Authors: | , , |
Format: | Article |
Language: | English |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | Acidic mine waters represent natural effluents from pyritic ore deposits and they are mainly characterized by a low pH and a high concentration of metal ions such as Fe
3+, Zn
2+, Cu
2+, Mn
2+, A1
3+, Ca
2+, Mg
2+ and Na
+. The treatment of these waters is of great economic and ecological importance. The present study was targeted at the development of a reagentless and wasteless dual-temperature ion-exchange technique for concentrating copper from the natural acidic mine waters of Rio Tinto area (Huelva, Spain). The carboxylic ion exchanger (Lewatit R 250-K) and iminodiacetic resin (Lewatit TP-207) were used. Values of the resin capacity towards mine water metal ions and the equilibrium separation factors (α) for different metal ion couples have been determined at different temperatures in the range 20–80°C. Acrylic resin has been found to be selective for Al
3+ and iminodiacetic resin demonstrates high selectivity for Cu
2+. Furthermore, the sorbability of Al
3+ increases while that of Cu
2+ decreases with temperature for both resins. This effect gives the possibility for a selective thermostripping of Cu
2+ from the resins pre-equilibrated with cold mine water (at 20°C) using hot mine water at 80°C. The increase in the Cu
2+ concentration in the eluate is 30% for acrylic resin and 20% for iminodiacetic resin. The concentration of Al
3+ in the stripping solution drops to 50% in the first case and to 70% in the second. |
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ISSN: | 0304-386X 1879-1158 |
DOI: | 10.1016/S0304-386X(96)00056-4 |