Method of removing impurities out of nickel chloride leachate
A technology of nickel chloride and leaching solution, which is applied in the field of non-ferrous metal smelting, and can solve the problems of insufficient separation of nickel ions and impurity metal ions
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Embodiment 1
[0020] Use 33% concentrated hydrochloric acid as the leaching agent to leaching the nickel-cobalt hydroxide raw material, the liquid-solid mass ratio of the concentrated hydrochloric acid to the nickel-cobalt hydroxide material is 1.0:1, acid leaching for 1.5 hours at a temperature of 80°C, and control the leaching end point pH to 3.5, filter to obtain nickel chloride leaching solution; take sulfonated kerosene as diluent, add sulfonated kerosene in p-507 until the concentration of p-507 is 0.73mol / L, take 10.0L p-507 concentration as 0.73mol / L organic solvent, add 500mL of 30% NaOH solution to react, carry out phase separation, the water phase is discharged to the waste water treatment system, and the sodium soap organic phase obtained after phase separation is mixed with 3000mL Ni 2+ Concentration is the reaction of the nickel chloride solution of 50.14g / L, carries out phase separation after the reaction, and after the phase separation, the water phase is discharged into the ...
Embodiment 2
[0022] Use 34% concentrated hydrochloric acid as the leaching agent to leach the nickel-cobalt hydroxide raw material, the liquid-solid mass ratio of the concentrated hydrochloric acid to the nickel-cobalt hydroxide material is 1.2:1, and acid leaching for 1.3 hours at a temperature of 70°C to control the leaching End point pH to 4.0, filter to obtain nickel chloride leaching solution; use sulfonated kerosene as diluent, add sulfonated kerosene to p-507 until the concentration of p-507 is 0.77mol / L, take 10.0L p-507 concentration It is 0.77mol / L organic solvent, add 500mL of 30% NaOH solution successively to react, carry out phase separation, and the water phase is discharged to the wastewater treatment system, and the sodium soap organic phase obtained after phase separation is then mixed with Ni 2+ Concentration is 62.47g / L nickel sulfate solution 3000mL reaction, carry out phase separation after the reaction, the water phase is discharged outside the waste water treatment sy...
Embodiment 3
[0024] Use 35% concentrated hydrochloric acid as the leaching agent to leach the nickel-cobalt hydroxide raw material, the liquid-solid mass ratio of the concentrated hydrochloric acid to the nickel-cobalt hydroxide material is 1.5:1, acid leaching for 1.0 hour at a temperature of 60°C, and control the leaching end point pH to 3.8, filter to obtain nickel chloride leaching solution; take sulfonated kerosene as diluent, add sulfonated kerosene to p-507 until the concentration of p-507 is 0.74mol / L, take 10.0L p-507 concentration as 0.74mol / L organic solvent, sequentially add 500mL of 30% NaOH solution to react, carry out phase separation, the water phase is discharged to the wastewater treatment system, and the sodium soap organic phase obtained after phase separation is then mixed with Ni 2+Concentration is 99.79g / L nickel sulfate solution 2000mL reaction, carry out phase separation, after phase separation, the water phase is discharged to the waste water treatment system, and ...
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