A clean production method for the separation and comprehensive utilization of iron, nickel, cobalt and silicon in the process of hydrochloric acid atmospheric leaching of laterite nickel ore
A technology for the separation of laterite nickel ore and silicon, which is applied in the process of hydrochloric acid atmospheric leaching of laterite nickel ore, iron and nickel, separation and comprehensive utilization of silicon, and cobalt fields. problems, to achieve the effect of solving difficult processing and reducing the cost of raw materials
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Embodiment 1
[0040] Use limonite-type lateritic nickel ore as raw material, grind it, the particle size is controlled at 200 mesh, and the ore amount accounts for 90% of the total ore amount. After grinding, add 36% hydrochloric acid to the enamel reaction kettle at the acid ore mass ratio of 1:1 Mix and heat up, and start timing the reaction when the temperature reaches 100°C. After the reaction, the plate and frame filter press is carried out. The main elements in the acid leaching solution are: Fe: 120.7g / L, Ni: 2.88g / L, Co: 0.19g / L, Cr: 2.89g / L, Al: 5.98g / L, Mg: 3.03g / L. Then use serpentine-type laterite nickel ore as raw material, grind it, the particle size is controlled at 200 mesh, and the ore amount accounts for 90% of the total ore amount. After grinding, it is added to the homogeneous reaction with the above-mentioned leaching solution according to the acid ore mass ratio of 1:1. Mix and heat up in the kettle, and start timing the reaction when the reaction reaches 150°C. Aft...
Embodiment 2
[0042] Use limonite-type lateritic nickel ore as raw material, grind it, the particle size is controlled at 200 mesh, and the ore amount accounts for 90% of the total ore amount. After grinding, add 20% hydrochloric acid to the enamel reaction kettle at the acid ore mass ratio of 5:1 Mix and heat up, and start timing the reaction when the temperature reaches 60°C. After the reaction, plate and frame filter press is carried out. The main elements in the acid leaching solution are: Fe: 100.12g / L, Ni: 2.06g / L, Co: 0.1g / L, Cr: 1.67g / L, Al: 3.99g / L, Mg: 2.06g / L. Then use serpentine-type lateritic nickel ore as raw material, grind it, the particle size is controlled at 200 mesh, and the amount of ore accounts for 90% of the total ore amount. After grinding, it is added to the homogeneous reaction with the above-mentioned leaching solution according to the acid ore mass ratio of 2:1. Mix and heat up in the kettle, and start timing the reaction when the reaction reaches 120°C. Afte...
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