Recovery method of rough ferro-nickel alloy and application of recovery method
A recovery method and a nickel-iron alloy technology are applied in the recovery field of crude nickel-iron alloys, which can solve the problems of iron concentrates with a purity of less than 80%, and achieve the effects of simple operation, easy control of technical conditions, and short technological process.
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Embodiment 1
[0041] The recovery method of the crude nickel-iron alloy of the present embodiment may further comprise the steps:
[0042] (1) Crude nickel-iron alloy (from a laterite nickel ore processing plant product in Indonesia) (composition in the crude nickel-iron alloy is: Fe 64%, Ni 33%, C 1.2%, S 1.7%) 100g is broken, and then Use a ball mill to mill until the particle size of the nickel-iron alloy is less than 100 mesh (>95%);
[0043] (2) The ammonia water and ammonium sulfate system is configured into a leachate, and added to the nickel-iron alloy after ball milling, the liquid-solid ratio of the leachate and the nickel-iron alloy is 3:1mL / g, and the total ammonia concentration is 6mol / L, wherein the sulfate radical and the ammonia The root molar concentration ratio is 1:2, put it into a closed reaction container, and the stirring speed is 400r / min. After 30 minutes of reaction, start to pass the air and heat it. After the reaction, the pH of the slurry is detected to be 9.8, ...
Embodiment 2
[0054] The recovery method of the crude nickel-iron alloy of the present embodiment may further comprise the steps:
[0055] (1) Take 100g of crude nickel-iron alloy (from a laterite nickel ore processing plant in Indonesia) (the composition of the nickel-iron alloy is: Fe64%, Ni 33%, C 1.2%, S 1.7%) 100g is crushed, and then ball mill is used Ball milling until the particle size of the nickel-iron alloy is less than 100 mesh (the particle size is less than 100 mesh and the proportion is >95%);
[0056] (2) The aqueous ammonia and ammonium sulfate system is configured into a leach solution, which is added to the above-mentioned nickel-iron alloy after ball milling. The liquid-solid ratio of the leach solution and the nickel-iron alloy is 4:1mL / g, and the total ammonia concentration is 5mol / L, wherein the sulfate radical and the ammonia The root molar concentration ratio is 1:3, put it into a closed reaction container, and the stirring speed is 400r / min. After the reaction for ...
Embodiment 3
[0066] The recovery method of the crude nickel-iron alloy of the present embodiment may further comprise the steps:
[0067] (1) Get the crude nickel-iron alloy (the composition in the nickel-iron alloy is: Fe 64%, Ni 33%, C 1.2%, S 1.7%) 100g is crushed, and then ball milled by a ball mill until the nickel-iron alloy particle size is less than 100 mesh (grain diameter less than 100 meshes accounted for >95%);
[0068] (2) The ammonia water and ammonium sulfate system is configured into a leach solution, and added to the nickel-iron alloy after ball milling, the liquid-solid ratio of the leach solution and the nickel-iron alloy is 5:1mL / g, and the total ammonia concentration is 7mol / L, wherein the sulfate radical and the ammonia The root molar concentration ratio is 1:4, wherein the solution pH=10.8 is recorded, put it into a closed reaction vessel, and the stirring speed is 500r / min, and after 30 minutes of reaction, air is started and heated, the flow rate of the air is 2.5L...
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