Process for separating copper and cobalt in alloy leaching solution and recycling sulfuric acid in solution
A technology for separating alloys and recovering solutions, applied in the field of hydrometallurgy and chemical industry, can solve problems such as acid waste, and achieve the effects of reducing production costs, shortening the technological process, and easily controlling the production process
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Embodiment 1
[0016] Composition: Cu 70g / L, Co 30g / L, Fe 0.095g / L, H 2 SO 4 2L of 15g / L alloy leaching solution, after 20 hours of conventional electrowinning and 5 hours of cyclone electrowinning, the composition of the leaching solution is: Cu 0.2g / L, Co 29.91g / L, Fe 0.08g / L, H 2 SO 4 120g / L, then the solution was evaporated and concentrated, and after evaporation, it was separated by suction filtration to obtain 132.8g of cobalt yellow residue containing 37.5% Co, and the concentrated solution component was H 2 SO 4 510g / L, Co 21.7g / L sulfuric acid concentrated solution 470ml.
[0017] The recovery rate of comprehensive sulfuric acid is over 99%. The output rate of cobalt is >80%.
Embodiment 2
[0019] Composition: Cu 30g / L, Co 15g / L, Fe 0.087g / L, H 2 SO 4 13g / L alloy leaching solution 2L, after conventional electrowinning for 12 hours and swirl electrowinning for 5 hours, the composition of the leaching solution is: Cu 0.26g / L, Co 14.89g / L, Fe 0.064g / L, H 2 SO 4 58g / L, then the solution was evaporated and concentrated, and after evaporation, it was separated by suction filtration to obtain 69.1g of cobalt yellow residue containing 36.8% Co, and the concentrated solution component was H 2 SO 4 305g / L, 380ml of concentrated sulfuric acid solution of Co 12g / L.
[0020] The recovery rate of comprehensive sulfuric acid is over 99%. The output rate of cobalt is >84%.
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