Strengthened leaching method of nickel in molybdenum sulfide nickel ores
A technology of enhanced leaching and molybdenum sulfide, applied in the direction of improving process efficiency, can solve problems such as environmental pollution, comprehensive recovery, and unsatisfactory beneficiation effects, and achieve the effects of low equipment requirements, saving raw materials, and low risk
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Embodiment 1
[0029] (1) Roasting: Grind the ore sample to below 0.0061mm, take 800g, add 720g of anhydrous sodium carbonate according to the ratio of 1:0.9, and roast at 560°C for 6h. During the roasting process, introduce air and stir every 30min. Then raise the temperature to 650°C and roast for 1.5h to obtain 1344g calcined sand. After analysis, the grade of nickel in the calcined sand is 2.67%, the recovery rate of nickel is 96.70%, the grade of molybdenum is 3.50%, and the recovery rate is 99.85%.
[0030] (2) Separation of molybdenum and nickel: the calcined sand obtained in step (1) is ground by a vibrating mill at 960r / min for 3min, and the particle size is 0.076mm. Water immersion adopts a liquid-solid ratio of 4:1, leaching temperature of 95°C, time of 2h, filtering and washing to obtain a dark gray filter residue, which contains 4.51% nickel, and the recovery rate of nickel is 99.70%; after analysis, 95.43% of molybdenum enters the filtrate.
[0031] (3) Enhanced leaching of ni...
Embodiment 2
[0033] (1) Roasting: Grind the ore sample until the particle size is below 0.01mm, add anhydrous sodium carbonate according to the mass ratio of 1:2, and roast at 530°C for 8h, then raise the temperature to 600°C, and roast for 3h, during the roasting process Introduce air and stir once every 20 minutes to obtain calcined sand. After analysis, the nickel grade in the calcined sand is 2.75%, the recovery rate of nickel is 96.59%, the grade of molybdenum is 3.53%, and the recovery rate is 99.91%.
[0034] (2) Separation of molybdenum and nickel: Grind the calcined sand obtained in step (1) at 900r / min for 5 minutes until the particle size is less than 0.1mm, and then immerse in water at a liquid-solid ratio of 2:1 at a leaching temperature of 70°C. After 3 hours, filter and wash to obtain dark gray filter residue, which contains 4.57% nickel, and the recovery rate of nickel is 99.81%; after analysis, 95.57% of molybdenum enters the filtrate.
[0035] (3) Enhanced leaching of nic...
Embodiment 3
[0037] (1) Roasting: Grind the ore sample until the particle size is below 0.008mm, add anhydrous sodium carbonate according to the mass ratio of 2:1, roast at 600°C for 4h, then raise the temperature to 800°C, and roast for 1h, during the roasting process Air was introduced and stirred every 40 minutes to obtain calcined sand. After analysis, the nickel grade in the calcined sand was 2.59%, the recovery rate of nickel was 96.67%, the grade of molybdenum was 3.52%, and the recovery rate was 99.81%.
[0038] (2) Separation of molybdenum and nickel: Grind the calcined sand obtained in step (1) at 1000 r / min for 1 min until the particle size is below 0.09 mm, and then immerse in water at a liquid-solid ratio of 8:1 at a leaching temperature of 100 °C. After 1h, filter and wash to obtain dark gray filter residue, which contains 4.50% nickel, and the recovery rate of nickel is 99.68%; after analysis, 95.41% of molybdenum enters the filtrate.
[0039] (3) Enhanced leaching of nickel...
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