Comprehensive recovery method of complex molybdenum sulphide ores
A recovery method and technology of sulfide ore, applied in the field of hydrometallurgy, can solve the problems of large alkali consumption, high energy consumption, and high cost, and achieve efficient oxidation and environmental friendliness
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Embodiment 1
[0028] Composition of molybdenum minerals used in pressurized oxidation (%): Mo44.95, Re0.062, S37.00
[0029] The pressure oxidation leaching conditions are as follows: take 100g of molybdenum concentrate, add 5g of activated carbon, the liquid-solid ratio is 2:1, the pressure oxidation temperature is 105°C, the oxygen partial pressure is 800kPa, and the reaction time is 8h. Analysis of the contents of each element in the pressurized leaching slag shows that the leaching rate of molybdenum is 17.25%, the leaching rate of rhenium is 96.47%, the content of sulfuric acid in the pressurized leaching solution is 131.48g / L, and the conversion rate of molybdenum is 99.12%.
Embodiment 2
[0031] Composition of molybdenum minerals used in pressurized oxidation (%): Mo44.95, Re0.062, S37.00
[0032] The pressure oxidation leaching conditions are: take 500g of molybdenum concentrate, add 25g of activated carbon, the liquid-solid ratio is 6:1, the pressure oxidation temperature is 150°C, the oxygen partial pressure is 700kPa, and the reaction time is 4h. Analysis of the content of each element in the pressurized leaching slag shows that the leaching rate of molybdenum is 22.25%, the leaching rate of rhenium is 96.47%, the content of sulfuric acid in the pressurized leaching solution is 131.48g / L, and the conversion rate of molybdenum is 98.50%.
Embodiment 3
[0034] Composition of molybdenum minerals used in pressure oxidation (%): Mo33.06, Cu5.72, Fe11.19, Re0.012, S40.08
[0035] The pressure oxidation leaching conditions are as follows: take 100g of molybdenum concentrate, add 2.5g of activated carbon, the liquid-solid ratio is 6:1, the pressure oxidation temperature is 180°C, the oxygen partial pressure is 600kPa, and the reaction time is 2.5h. Analysis of the content of each element in the pressurized leaching slag shows that the leaching rate of molybdenum is 22.41%, that of rhenium is 96.47%, that of copper is 99.65%, and that of iron is 96.25%. The content of sulfuric acid in the pressurized leaching solution is 146.26g / L, the conversion rate of molybdenum is 98.09%.
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