Clean production method for recovering uranium and molybdenum from wrapped uranium and molybdenum ores
A wrap-type, molybdenum ore technology, applied in the fields of chemical industry and metallurgy, can solve the problems of complex uranium and molybdenum metal recovery process, difficult solid-liquid separation of leaching slurry, and difficult solid-liquid separation, so as to save solid-liquid separation and save equipment costs. , The effect of operating environment friendly
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Embodiment 1
[0019] Crushing and grinding the uranium-molybdenum ore with uranium and molybdenum grades of 0.093% and 1.18% respectively to a particle size of less than -100 mesh, in which the sulfur content in the ore is 3.47%, mix it evenly according to the CaO / S molar ratio of 1.2, and then mix it with water for granulation , control the maximum particle size at 10mm, send it to the rotary kiln for roasting at 600°C for 3 hours, build up a heap and spray leaching after cooling, the concentration of sulfuric acid in the spraying leaching agent in the early stage of leaching is 120g / L, and the spraying intensity is 40L / ( m 2 h), the spraying time is 3 days; the concentration of sulfuric acid in the leaching agent in the later stage of leaching is 15g / L, spraying in intervals, spraying for 16 hours a day, and the spraying intensity is 20 / (m 2 h), the spraying time is 17 days.
[0020] After leaching, the slag analysis showed that the leaching rate of uranium was 90.1%, the leaching rate o...
Embodiment 2
[0022] Crush and grind uranium-molybdenum ore with uranium and molybdenum grades of 0.093% and 1.18% respectively to a particle size of less than -100 mesh, in which the sulfur content in the ore is 3.47%, and mix it evenly according to the CaO / S molar ratio of 1.5, then mix it with water and granulate , control the maximum particle size at 10mm, send it to the rotary kiln for roasting at 600°C for 3 hours, build up a heap and spray leaching after cooling, the concentration of sulfuric acid in the spraying leaching agent in the early stage of leaching is 120g / L, and the spraying intensity is 40L / ( m 2 h), the spraying time is 3 days; the concentration of sulfuric acid in the leaching agent in the later stage of leaching is 15g / L, spraying in intervals, spraying for 16 hours a day, and the spraying intensity is 20 / (m 2 h), the spraying time is 17 days.
[0023] After leaching, the slag analysis showed that the leaching rate of uranium was 90.2%, the rate of molybdenum leaching...
Embodiment 3
[0025] Crushing and grinding the uranium-molybdenum ore with uranium and molybdenum grades of 0.093% and 1.18% respectively to a particle size of less than -100 mesh, in which the sulfur content in the ore is 3.47%, mix evenly according to the CaO / S molar ratio of 2, and mix with water to granulate , control the maximum particle size at 10mm, send it to the rotary kiln for roasting at 600°C for 3 hours, build up a heap and spray leaching after cooling, the concentration of sulfuric acid in the spraying leaching agent in the early stage of leaching is 120g / L, and the spraying intensity is 40L / ( m 2 h), the spraying time is 3 days; the concentration of sulfuric acid in the leaching agent in the later stage of leaching is 15g / L, spraying in intervals, spraying for 16 hours a day, and the spraying intensity is 20 / (m 2 h), the spraying time is 17 days.
[0026] After leaching, the slag analysis showed that the leaching rate of uranium was 90.1%, the leaching rate of molybdenum was...
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