Method for extracting and separating nickel and molybdenum from nickel-molybdenum-containing coal gangue
A technology of stone coal mines and pellets, applied in the direction of improving process efficiency, etc., can solve problems such as high cost, long process, pollution, etc., and achieve the effects of saving production costs, high metal recovery rate, and comprehensive utilization
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Embodiment 1
[0034] The stone coal raw material used contains 4.5% molybdenum, 3.2% nickel, 22.3% sulfur, 12% carbon and 13.2% iron. The nickel-molybdenum ore is ground to -60 mesh, and mixed with sodium carbonate and sodium nitrate. The ratio is mineral powder: sodium carbonate: sodium nitrate = 100:87:0.20 and mixed in the mixer for 30 minutes. The mixture adopts a disc ball making mechanism Form Φ10-Φ20mm pellets. After drying, it is sent to an electric furnace for smelting at 1500°C, and the nickel-iron discharge temperature is 1600°C. The obtained reduction product nickel-iron alloy contains 52% nickel, phosphorus<0.06%, sulfur<0.03%, and the recovery rate of nickel is 96%. The molten slag is leached with water under the conditions of 80°C and a liquid-solid ratio of 3:1, and the molybdenum content in the leached slag is 0.2%.
[0035] The hot carbonation and cold carbonation treatment of the molybdenum-containing leachate are both carried out in the packed absorption tower, accordi...
Embodiment 2
[0037] The stone coal raw material used contains 3.5% molybdenum, 2.5% nickel, 18.5% sulfur, 12% carbon and 12% iron. The nickel-molybdenum ore is ground to -60 mesh, mixed with sodium carbonate and sodium nitrate, the ratio is mineral powder: sodium carbonate: sodium nitrate = 100:60:0, mixed in the mixer for 30 minutes, and the mixture is made of disc balls Machine made into Φ20-Φ25mm pellets. After drying, it is sent to an electric furnace for melting at 1500°C, and the nickel-iron discharge temperature is 1500°C. The obtained reduction product nickel-iron alloy contains 48% nickel, phosphorus<0.08%, sulfur<0.06%, and the recovery rate of nickel is 95%. The molten slag is leached with water under the conditions of 80°C and a liquid-solid ratio of 3:1, and the molybdenum content in the leached slag is 0.3%.
[0038] The hot carbonation and cold carbonation treatment of the molybdenum-containing leachate are both carried out in the packed absorption tower, according to the ...
Embodiment 3
[0040] The stone coal raw material used contains 5.8% molybdenum, 3.5% nickel, 28% sulfur, 15% carbon and 16% iron. The nickel-molybdenum ore is ground to -60 mesh, mixed with sodium carbonate and sodium nitrate, the ratio is mineral powder: sodium carbonate: sodium nitrate = 100: 110: 0.15, mixed in the mixer for 30 minutes, and the mixture is made into balls by discs Machine made into Φ20-Φ25mm pellets. After drying, it is sent to an electric furnace for smelting at 1600°C, and the nickel-iron discharge temperature is 1600°C. The obtained reduction product nickel-iron alloy contains 58% nickel, phosphorus2- 0.8 times the theoretical amount required for oxidation to sulfur is added to pyrolusite, the hot carbonation temperature is 80°C, the cold carbonation temperature is 30°C, the hot carbonation operating pressure is 6atm, and the carbonation time is 3 hours. The recovery rate of sulfur 80%, and the regeneration rate of soda is 82%.
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