Comprehensive treatment method for applying sodium-containing ammonium waste liquid to laterite nickel ore
A laterite nickel ore and comprehensive treatment technology, applied in the field of metallurgy, can solve the problems of high treatment costs, achieve the effects of reducing treatment costs, ensuring safe production, and avoiding spontaneous combustion
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Embodiment 1
[0026] Take 60L of saprolite ball mill slurry with a solid content of 33.5% and a 200-mesh screening rate of 97%, add 31.2kg of concentrated sulfuric acid, stir and react at 70°C for 2 hours to obtain a prepreg, and then place the prepreg in an oxygen autoclave for Oxygen pressure leaching, the total pressure is 1.2MPa, the leaching temperature is 180°C, and the leaching time is 2h, the nickel leaching rate is 95.96%, the impurity element iron: 7.16g / L, aluminum: 3.57g / L leach solution.
[0027] Add 35g / L of sodium sulfate and 20g / L of ammonium sulfate containing sodium ammonium waste liquid, and add calcium hydroxide to adjust the pH to 2.0, filter to remove the slag, and add 30% liquid caustic soda slurry to part of the neutralization solution to adjust pH to 5.0, filter to remove iron and aluminum slag, obtain impurity-removed liquid. Add liquid caustic soda to the impurity-removed liquid to adjust the pH to 8.0, stir and react for 6 hours, and obtain the nickel hydroxide c...
Embodiment 2
[0029]Take 60L of limonite ball mill slurry with a solid content of 33.5% and a 200-mesh sieving rate of 97%, add 32kg of concentrated sulfuric acid, stir and react at 80°C for 4 hours to obtain a prepreg, and then place the prepreg in an oxygen autoclave for Oxygen pressure leaching, the total pressure is 1.8MPa, the leaching temperature is 180°C, and the leaching time is 2h, the nickel leaching rate is 96.35%, the impurity element iron: 5.98g / L, aluminum: 2.57g / L leaching solution.
[0030] Add 35g / L of sodium sulfate and 20g / L of ammonium sulfate containing sodium ammonium waste liquid, and add calcium carbonate to adjust the pH to 2.0, filter to remove residue, add 15% calcium carbonate to part of the neutralization solution to adjust the pH to 4.8, filter The iron and aluminum slag is removed to obtain the impurity-removed liquid. Calcium oxide is added to the impurity-removed liquid to adjust the pH to 8.0, and the reaction is stirred for 6 hours to obtain the nickel hyd...
Embodiment 3
[0032] Take 60L of limonite ball mill slurry with a solid content of 33.5% and a 200-mesh sieving rate of 97%, add 32kg of concentrated sulfuric acid, stir and react at 90°C for 4 hours to obtain a prepreg, and then place the prepreg in an oxygen autoclave for Oxygen pressure leaching, the total pressure is 1.8MPa, the leaching temperature is 200°C, and the leaching time is 2h, the nickel leaching rate is 98.35%, the impurity element iron: 4.5g / L, aluminum: 0.57g / L leach solution.
[0033] Add sodium sulfate 20g / L, ammonium sulfate 8g / L sodium ammonium containing waste liquid, and add calcium carbonate to adjust the pH to 2.0, filter to remove residue, add 15% calcium carbonate to part of the neutralization solution to adjust the pH to 4.8, filter The iron and aluminum slag is removed to obtain the impurity-removed liquid. Magnesium oxide is then added to the impurity-removed liquid to adjust the pH to 7.8, and the reaction is stirred for 6 hours to obtain the nickel hydroxide...
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