A method of leaching scandium from scandium-rich material by preheating-step pressure
A material and leaching technology, applied in the field of high-pressure leaching of scandium and hydrometallurgy, can solve the problems of high cost and low leaching rate of scandium, and achieve the effects of less investment in equipment, saving grinding costs, and convenient transportation and storage.
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Embodiment 1
[0019] a. Put Sc 2 o 3 The scandium-rich material with a content of 82.6g / t is added to the wet ball mill at a slurry concentration of 55%, and the material that is ball-milled to less than 100 mesh accounts for 96.73%;
[0020] b. Adjust the concentration of the pulp from the grinding to 41.5%, and then inject the pulp into the high-pressure reactor;
[0021] c. Pressurize and inject air into the reaction kettle to make the pressure inside the kettle reach 0.3MPa, and preheat to 90°C;
[0022] d. Add concentrated sulfuric acid 1.1 times the weight of fine ore into the acid tank, inject concentrated sulfuric acid into the reactor at 0.7MPa, and keep the pressure inside the reactor at 0.7MPa;
[0023] e. Keep the temperature in the kettle at 130°C and hold for 4 hours;
[0024] f. Filtrate when the temperature in the kettle drops to 90°C to obtain scandium-containing leaching solution and leaching residue. At this time, the leaching rate is 88.19%.
Embodiment 2
[0026] a. Put Sc 2 o 3 The scandium-rich material with a content of 82.6g / t is added to the wet ball mill at a slurry concentration of 55%, and the material that is ball-milled to less than 100 mesh accounts for 98.22%;
[0027] b. Adjust the concentration of the ore pulp from the grinding to 45.5%, and then inject the ore pulp into the high-pressure reactor;
[0028] c. Pressurize and inject air into the reaction kettle to make the pressure inside the kettle reach 0.3MPa, and preheat to 90°C;
[0029] d. Add concentrated sulfuric acid 1.1 times the weight of fine ore into the acid tank, inject concentrated sulfuric acid into the reactor at 0.8MPa, and keep the pressure inside the reactor at 0.8MPa;
[0030] e. Keep the temperature in the kettle at 130°C and hold for 6 hours;
[0031] f. Filtrate when the temperature in the kettle drops to 90°C to obtain scandium-containing leaching solution and leaching residue. At this time, the leaching rate is 91.72%.
[0032] Table 1 ...
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