TY - JOUR
T1 - Dissolution of copper and nickel from nickel-rich anode slimes under oxidized pressure leaching
AU - Mohanty, Udit S.
AU - Kalliomäki, Taina
AU - Seisko, Sipi
AU - Peng, Chao
AU - Rintala, Lotta
AU - Halli, Petteri
AU - Aromaa, Jari
AU - Taskinen, Pekka
AU - Lundström, Mari
PY - 2019/1/1
Y1 - 2019/1/1
N2 - Anode slimes are valuable by-products in the electrolytic copper refinery process. This study aimed to investigate maximum extraction efficiency of Cu and Ni from slimes originating from the electrorefining of anodes containing high [Ni]. In addition, the extractions of Se, Te, As and Bi were determined. A factorial leaching series was conducted with T = 140–160°C, [H2SO4] = 12–20%, pO2= 2–8 bars and solid/liquid ratio = 200–400 g/L. The highest Ni extraction of 99.7% was obtained with [H2SO4] = 20%, pO2 = 8 bar and T = 160°C while maintaining S/L ratio of 200 g/L. The extraction of copper was found to be within 97–99% in all the leaching experiments. Increasing acidity and decreasing S/L ratio increased the efficiency of Cu extraction. Mineralogical characterizations by SEM-EDX demonstrated the presence of Ag2Se, BaSO4, PbSO4 and several oxide phases in the leach residue.
AB - Anode slimes are valuable by-products in the electrolytic copper refinery process. This study aimed to investigate maximum extraction efficiency of Cu and Ni from slimes originating from the electrorefining of anodes containing high [Ni]. In addition, the extractions of Se, Te, As and Bi were determined. A factorial leaching series was conducted with T = 140–160°C, [H2SO4] = 12–20%, pO2= 2–8 bars and solid/liquid ratio = 200–400 g/L. The highest Ni extraction of 99.7% was obtained with [H2SO4] = 20%, pO2 = 8 bar and T = 160°C while maintaining S/L ratio of 200 g/L. The extraction of copper was found to be within 97–99% in all the leaching experiments. Increasing acidity and decreasing S/L ratio increased the efficiency of Cu extraction. Mineralogical characterizations by SEM-EDX demonstrated the presence of Ag2Se, BaSO4, PbSO4 and several oxide phases in the leach residue.
KW - Autoclave
KW - copper electrorefining
KW - extraction efficiency
KW - hydrometallurgy
KW - modelling
KW - secondary metal sources
KW - sulphuric acid leaching
KW - valorization
UR - http://www.scopus.com/inward/record.url?scp=85073975373&partnerID=8YFLogxK
U2 - 10.1080/25726641.2019.1670008
DO - 10.1080/25726641.2019.1670008
M3 - Article
AN - SCOPUS:85073975373
SN - 2572-6641
JO - Mineral Processing and Extractive Metallurgy: Transactions of the Institute of Mining and Metallurgy
JF - Mineral Processing and Extractive Metallurgy: Transactions of the Institute of Mining and Metallurgy
ER -