Purification method of cobalt nickel hydroxide hydrochloric acid leaching solution
A technology of nickel-cobalt hydroxide hydrochloric acid and leaching solution, applied in the purification of leaching solution, the purification of nickel-cobalt hydroxide hydrochloric acid leaching solution, and the production of nickel chloride products, can solve the problems such as the failure of nickel chloride to be popularized, and achieve the elimination of major dangers The effect of shortening the source and process flow and preventing pollution
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Embodiment 1
[0026] A method for purifying nickel hydroxide cobalt hydrochloric acid leaching solution, comprising the following process steps:
[0027] Step 1: Use industrial concentrated hydrochloric acid with a molar concentration of 8mol / L to dissolve and leach the nickel cobalt hydroxide raw material produced by the transformation of laterite nickel ore, control the pH value of the leached solution to 4.3, and then filter the solution to obtain nickel A leach solution with a content of 150g / L;
[0028] Step 2: adding barium chloride to the leaching solution to carry out the sulfate removal operation, after the sulfate removal, the solution is press-filtered and used as the pre-extraction liquid for subsequent use; the amount of barium chloride added is calculated according to the sulfate content of the sulfate removal pre-liquid, Ensure that the sulfate content in the solution after removing the sulfate is below 20g / L;
[0029] Step 3: Follow the P 507 : Sulfonated kerosene=25%:...
Embodiment 2
[0033] The difference between embodiment 2 and embodiment 1 is:
[0034] In step 1, the nickel hydroxide cobalt raw material produced by the transformation of laterite nickel ore is dissolved and leached by industrial concentrated hydrochloric acid with a molar concentration of 9 mol / L, and the pH value of the leached solution is controlled to be 4.5, and then the solution is press-filtered to obtain The leach solution with a nickel content of 164g / L;
[0035] In step 3, according to sodium saponification rate 70%, metering and adding mass concentration is the sodium hydroxide solution of 30% to carry out saponification, and the organic phase after saponification reacts with the pure nickel chloride solution of nickel content at 100g / L to make nickel soap;
[0036] In step 4, be that the dilute hydrochloric acid of 0.5mol / L carries out 3 grades of washing sodium to the nickel soap that step 3 makes with molar concentration, to remove the sodium ion in the liquid after nic...
Embodiment 3
[0038] The difference between embodiment 3 and embodiment 1 is:
[0039] In step 1, the nickel cobalt hydroxide raw material produced by the transformation of laterite nickel ore is dissolved and leached by industrial concentrated hydrochloric acid with a molar concentration of 10 mol / L, and the pH value of the leached solution is controlled to be 4.0, and then the solution is press-filtered to obtain Leaching solution with a nickel content of 170g / L;
[0040] In step 3, according to sodium saponification rate 75%, metering and adding mass concentration is 30% sodium hydroxide solution to carry out saponification, and the organic phase after saponification reacts with the pure nickel chloride solution of nickel content at 110g / L to make nickel soap;
[0041] In step 4, be that the dilute hydrochloric acid of 1.0mol / L carries out 3 grades of washing sodium to the nickel soap that step 3 makes with molar concentration, to remove the sodium ion in the liquid after nickel soap, a...
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