A Nitric Acid Route in Combination with Solvent Extraction for. Hydrometallurgical Treatment of Chalcopyrite

- Organization:
- The Minerals, Metals and Materials Society
- Pages:
- 13
- File Size:
- 259 KB
- Publication Date:
- Jan 1, 1976
Abstract
After complete dissolution of chalcopyrite concentrate in sulphuric acid in presence of nitric acid the excess of the latter is expelled by a surplus of concentrate and the last traces of nitrate removed in the mother liquor after crystallization of the copper and iron sulphates. Zinc accumulates in the mother liquor from which it can be removed by solvent extraction of zinc sulphate as a pair of ions. After dissolution of the sulphate crystals in water the neutral solution is oxidized in an autoclave at 140°C where iron sulphate is thermally hydrolyzed; the iron-free solution is taken to copper electrowinning and the cell acid after partial evaporation recirculated with the mother liquor to the leaching circuit. Total recovery of copper is about 96%; other metals like zinc and iron are concentrated in industrially usable products. At a copper price of about 70 c/lb, the method appears to be profitable also in a small unit.
Citation
APA:
(1976) A Nitric Acid Route in Combination with Solvent Extraction for. Hydrometallurgical Treatment of ChalcopyriteMLA: A Nitric Acid Route in Combination with Solvent Extraction for. Hydrometallurgical Treatment of Chalcopyrite. The Minerals, Metals and Materials Society, 1976.