Method for leaching nickel and molybdenum from amorphous nickel-molybdenum sulfide mineral by oxidative conversion
A nickel-molybdenum sulfide and amorphous technology, which is applied in the field of metallurgy and chemical industry, can solve the problem of not making full use of the specific surface area of amorphous nickel-molybdenum sulfide ore, and achieve high metal leaching rate, large specific surface area and short process flow. Effect
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Embodiment 1
[0017] Example 1: The mass percentages of the main chemical components of amorphous nickel-molybdenum sulfide ore are Ni 11.5%, Mo 2.0%, and S 30.5%, and the corresponding minerals are crushed and finely ground to a particle size of less than 0.1mm, accounting for 80%. Take 5kg of finely ground ore samples, mix them with 7.5L of water to make slurry (liquid-solid ratio is 1.5:1), and use an acid-resistant pump to pump the ore slurry into the autoclave. Introduce industrial oxygen into the kettle to keep the pressure in the kettle at 0.8MPa; turn on the heating system to heat up the pulp in the kettle, control the temperature to 110°C, react for 360min, and the acidity of the solution at the end of the reaction is 60g / L; discharge the pulp, filter, A leaching solution and leaching residue containing nickel sulfate and molybdenum sulfate are obtained. The leached slag was dried to obtain 1.95 kg of dry slag, corresponding to the chemical composition of the slag being Ni 1.27%, M...
Embodiment 2
[0019] Example 2: The mass percentages of the main chemical components of amorphous nickel-molybdenum sulfide ore are Ni 6.2%, Mo 5.1%, and S 21.8%, and the corresponding minerals are crushed and finely ground to a particle size of less than 0.1mm, accounting for 80%. Take 3.5kg of finely ground ore samples, mix them with 7.0L of water (liquid-solid ratio is 2:1), and pump the ore slurry into the autoclave with an acid-resistant pump. Introduce industrial oxygen into the kettle to keep the pressure inside the kettle at 1.2MPa; turn on the heating system to raise the temperature of the pulp in the kettle, control the temperature to 125°C, react for 300 minutes, and the acidity of the solution after the reaction is 30g / L; discharge the pulp, filter, A leaching solution and leaching residue containing nickel sulfate and molybdenum sulfate are obtained. The leached slag was dried to obtain 2.21 kg of dry slag, corresponding to the mass percentages of the chemical components of the...
Embodiment 3
[0021] Example 3: The mass percentages of the main chemical components of the amorphous nickel-molybdenum sulfide ore are Ni 3.0%, Mo 9.8%, and S 8.0%, and the corresponding minerals are crushed and finely ground until the particle size is less than 0.1 mm, accounting for 80%. Take 1.5kg of finely ground ore sample, mix it with 7.5L of water to adjust slurry (liquid-solid ratio is 5:1), and use an acid-resistant pump to pump the slurry into the autoclave. Introduce industrial oxygen into the kettle to keep the pressure in the kettle at 2.0MPa; turn on the heating system to heat up the pulp in the kettle, control the temperature to 200°C, and react for 180 minutes to finish the reaction. The acidity of the solution is 5g / L; discharge the pulp and filter to obtain Leaching solution and leaching residue containing nickel sulfate and molybdenum sulfate. The leached slag was dried to obtain 0.92 kg of dry slag, corresponding to the mass percentages of the chemical components of the...
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