Electrolytic manganese slag source decrement method
A technology of electrolytic manganese slag and source, applied in the field of hydrometallurgical clean production, can solve problems such as failure to consider high moisture content of manganese slag
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Embodiment 1
[0017] Take 50 kg of manganese carbonate ore powder, add 250 L of water according to the solid-to-liquid ratio of 1:5 to obtain the ore slurry, place the ore slurry on the reactor, add 90 mg of sodium oleate, and then add 13 L of 98% concentrated sulfuric acid. Control the temperature at 65°C and continue stirring. After 3.5 hours of leaching reaction, calcium oxide is added to the leached ore slurry according to the solid-to-liquid ratio to adjust the pH value to 6.6. After 1 hour of reaction, the manganese-containing solution and manganese slag are obtained through a filter press. In this example, 230 L of manganese-containing solution was finally obtained. The leaching rate of manganese was 82.23%, and the moisture content of manganese slag was 26.50%. .
Embodiment 2
[0019] Take 50 kg of manganese carbonate ore powder, add 225 L of water according to the solid-to-liquid ratio of 1:4.5 to obtain the ore slurry, place the ore slurry on the reactor, add 100 mg of trisodium citrate, and then add 12.5 L of 98% of concentrated sulfuric acid. Control the temperature at 55°C and continue stirring. After 4.5 hours of leaching reaction, add calcium carbonate and calcium oxide to the leaching slurry according to the solid-to-liquid ratio and react for 2 hours to adjust the pH value to 7. Manganese-containing solution and manganese slag are obtained through a filter press. In this example, 236 L of manganese-containing solution was finally obtained. The leaching rate of manganese was 98.08%, and the moisture content of manganese slag was 23.2%. .
Embodiment 3
[0021] Take 50 kg of manganese carbonate ore powder, add 250 L of water according to the solid-to-liquid ratio of 1:5 to obtain the ore slurry, place the ore slurry on the reactor, add 50 mg of sodium lauryl sulfate, and then add 12.5 L of 98% concentrated sulfuric acid. Control the temperature at 55°C and continue stirring. After 4.5 hours of leaching reaction, add ammonia water and calcium oxide to the leaching slurry according to the solid-to-liquid ratio and react for 2.5 hours to adjust the pH value to 7. Manganese-containing solution and manganese slag are obtained through a filter press. In this example, 231 L of manganese-containing solution was finally obtained. The leaching rate of manganese was 90.00%, and the moisture content of manganese slag was 24.38%. .
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