Method for extracting molybdenum, nickel, vanadium and ferrum from polymetallic black-shale paragentic minerals
A technology for black shale and symbiotic ore is applied in the field of extracting molybdenum, nickel, vanadium, and iron, which can solve the problems of generating a large amount of flue gas, few components, and complicated process operations, and achieves the reduction of environmental pollution, the strengthening of metallurgical processes, and the simplicity of the process. Effect
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Embodiment 1
[0031] The composition of polymetallic black shale paragenetic ore is: molybdenum 3.78%, nickel 1.92%, vanadium 0.83%, iron 11.8%, sulfur 21.3%. Add 2T of finely ground polymetallic ore (300 mesh ≥ 90%) and 7T of water into a 10,000L closed reactor, heat the polymetallic black shale symbiotic ore to 200°C, and feed compressed air at a pressure of 2MPa. Under the agitation of high speed (200r / min) in the kettle, the oxidation leaching temperature was controlled at 200°C, and the reaction was carried out for 5 hours. After the reaction, it was filtered to obtain a total of 8.5T of filtrate and washing liquid, and a total of 4.5T of leached wet residue (water content 69%). Composition: molybdenum: 4.63g / L, nickel 3.94g / L, vanadium 1.53g / L, iron 21.8g / L; main components of the leaching slag after drying: molybdenum 2.79%, nickel 0.13%, vanadium 0.12%, iron 1.7 %, during the pressure oxidation leaching process, 95.4% of nickel, about 91% of vanadium, iron and about 50% of molybdenu...
Embodiment 2
[0038] Add 2T of finely ground polymetallic ore (300 mesh ≥ 90%) and 6T of water into a 10,000L closed reactor. The composition of polymetallic black shale paragenetic ore is: molybdenum 7.05%, nickel 3.93%, vanadium 0.73%, iron 13.8%, sulfur 18.7%. Heat the polymetallic black shale symbiotic ore to 250°C, feed compressed air at a pressure of 2.5MPa, control the oxidation leaching temperature to 250°C under stirring at a high speed (200r / min) in the autoclave, and react for 4 hours. Filtrate to obtain a total of 7.6T of filtrate and washing liquid, and a total of 3.5T of leached wet residue (water content 59%). The components of the leachate: molybdenum 11.13g / L, nickel 9.98g / L, vanadium 1.82g / L, iron 34.5g / L The main components of the leaching slag after drying: 3.93% molybdenum, 0.19% nickel, 0.05% vanadium, 0.96% iron, 95.4% nickel, about 95% vanadium, iron and about 50% molybdenum in the process of pressure oxidation leaching After entering the leach solution, the remaini...
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