Method for recovering copper from copper smelting anode furnace refining slag
A refining slag and anode furnace technology, which is applied in the field of copper recovery from the copper smelting anode furnace refining slag, can solve the problems of reducing the economic benefits of enterprises, and achieve the effects of wide application range, less pollution, and low energy consumption
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0028] A method for recovering copper from the anode furnace copper smelting slag refining, the specific steps are:
[0029] Containing Cu, Fe, Si, O, As, Zn, P, Pb, Ca, Co, Mn, respectively, 40.00%, 15%, 15%, 15%, 3.50%, 3.00%, 3.00%, 2%, 2 %, 0.50%, 1% of the refining slag pulverized, ground to a particle size less than 200 mesh, added containing As, Cu, Zn, H 2 SO 4 Respectively 4.56g / L, 0.56g / L, 0.95g / L and leaching is oxidized 1.52mol / L of spent acid. In the leaching conditions of temperature 80 ℃, liquid-solid ratio (ml / g) 6: 1, time 3h, the air rate of 100ml / min, the leaching rate of 75.02% Cu. Leaching residue was washed, dried 105 deg.] C, according to leach residue and the mass ratio of CaO 5.52: 1 mixture, at a temperature of 700 deg.] C, 4h calcination conditions at the time. After firing the resultant calcine leaching conditions of temperature 70 ℃, liquid to solid ratio of 4: 1, time 4h, under / min air rate 150ml oxidative leaching conditions again, leac...
Embodiment 2
[0031] A method for recovering copper from the anode furnace copper smelting slag refining, the specific steps are:
[0032] Containing Cu, Fe, Si, O, As, Zn, P, Pb, Ca, Co, Mn, respectively 20.03%, 24.97%, 25.00%, 19.94%, 2.26%, 0.98%, 2.01%, 1.25%, 1.98 %, 1.02%, 0.56% of the refining slag pulverized, ground to a particle size less than 200 mesh, added containing As, Cu, Zn, H 2 SO 4 7.79g / L, 1.98g / L, 0.5g / L for oxidative leaching and 0.56mol / L of spent acid, respectively. In the leaching conditions of a temperature of 40 ℃, liquid-solid ratio (ml / g) 8: 1, the time 1h, the air rate of 400ml / min, to give Cu leaching rate of 65.32%. Leaching residue was washed, dried 105 deg.] C, according to leach residue and the mass ratio of CaO 4: mixed with CaO. 1, at a temperature of 900 ℃, the firing conditions for 2h. After firing the resultant calcine leaching conditions of temperature 90 ℃, liquid to solid ratio of 6: 1, time 2h, under / min air rate 300ml oxidative leaching ...
Embodiment 3
[0034] A method for recovering copper from the anode furnace copper smelting slag refining, the specific steps are:
[0035] Containing Cu, Fe, Si, O, As, Zn, P, Pb, Ca, Co, Mn, respectively 29.95%, 19.96%, 19.91%, 25.01%, 1.01%, 1.98%, 0.98%, 0.51%, 0.49 %, 0.1%, 0.1% refining slags crushed, ground to a particle size less than 200 mesh, added containing As, Cu, Zn, H 2 SO 4 1.24g / L, 0.58g / L, 0.24g / L and leaching is oxidized 2.45mol / L of spent acid, respectively. In the leaching conditions of a temperature of 60 ℃, liquid-solid ratio (ml / g) 4: 1, time 5h, the air rate of 250min / ml, obtained leaching rate of 72.06% Cu. Leaching residue was washed, dried 105 deg.] C, more than 4.67 mass according to leach residue and CaO: CaO mixed and after 1, at a temperature of 500 ℃, 6h under calcination time. After firing the resultant calcine leaching conditions of temperature 50 ℃, liquid to solid ratio of 8: 1, Time 6h, an air rate of 400min / ml oxidative leaching conditions aga...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
