Method for preprocessing wrapped uranium-molybdenum ores through oxidizing roasting
An oxidative roasting and wrapping technology, applied in the field of uranium-molybdenum ore processing, can solve the problems of high operation and maintenance costs, difficult solid-liquid separation of ore slurry, high processing and manufacturing requirements, and achieves low impurity content in solution, low reagent consumption, The effect of low production cost
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Embodiment 1
[0019] A packaged uranium-molybdenum ore in a certain place, the main chemical components of the original ore are uranium grade of 0.106% and molybdenum grade of 1.26%.
[0020] (1) crushing and finely grinding the wrapped uranium-molybdenum ore to a particle size of -100 mesh;
[0021] (2) directly roasting the crushed and finely ground uranium-molybdenum ore of step (1), the roasting temperature is 600 DEG C, and the roasting time is 10min to obtain calcine;
[0022] (3) After cooling the calcine, use a sulfuric acid solution with a concentration of 80g / L to carry out stirring leaching at 60°C, the leaching time is 2h, the leaching liquid-solid ratio is 1:1, and then the leaching pulp is subjected to solid-liquid separation;
[0023] (4) performing solvent extraction on the solution obtained in step (3) to extract uranium and molybdenum.
[0024] The results showed that the leaching rate of uranium was 91.4%, and the leaching rate of molybdenum was 84.5%.
Embodiment 2
[0026] A packaged uranium-molybdenum ore in a certain place, the main chemical components of the original ore are uranium grade of 0.154% and molybdenum grade of 1.03%.
[0027] (1) crushing and finely grinding the wrapped uranium-molybdenum ore to a particle size of -60 mesh;
[0028] (2) directly roasting the crushed and finely ground uranium-molybdenum ore in step (1), the roasting temperature is 550°C, and the roasting time is 15min to obtain calcine;
[0029] (3) After cooling the calcine, use a sulfuric acid solution with a concentration of 100g / L to carry out stirring leaching at 60°C, the leaching time is 2h, the leaching liquid-solid ratio is 1:1, and then the leaching pulp is subjected to solid-liquid separation;
[0030] (4) performing solvent extraction on the solution obtained in step (3) to extract uranium and molybdenum.
[0031] The results showed that the leaching rate of uranium was 94.6%, and the leaching rate of molybdenum was 84.3%.
Embodiment 3
[0033] A parcel-type uranium-molybdenum ore in a certain place, the main chemical components of the original ore are uranium grade of 0.08% and molybdenum grade of 1.47%.
[0034] (1) crushing and finely grinding the wrapped uranium-molybdenum ore to a particle size of -150 mesh;
[0035] (2) directly roasting the crushed and finely ground uranium-molybdenum ore in step (1), the roasting temperature is 550°C, and the roasting time is 3min to obtain calcine;
[0036] (3) After cooling the calcine, use a sulfuric acid solution with a concentration of 100g / L to carry out stirring leaching at 20°C, the leaching time is 2h, the leaching liquid-solid ratio is 1.5:1, and then the leaching pulp is subjected to solid-liquid separation;
[0037] (4) performing solvent extraction on the solution obtained in step (3) to extract uranium and molybdenum.
[0038] The results showed that the leaching rate of uranium was 90.5%, and the leaching rate of molybdenum was 87.3%.
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