Method of preparing nickel nitrate by taking rough nickel hydroxide produced by laterite-nickel ore as raw material
A technology of nickel hydroxide and nickel nitrate, applied in chemical instruments and methods, nickel compounds, inorganic chemistry, etc.
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Embodiment 1
[0031] A method for preparing nickel nitrate from the thick nickel hydroxide produced by laterite nickel ore, comprising the following steps:
[0032] a. Preparation of Nickel Chloride Solution
[0033] The crude nickel hydroxide produced from laterite nickel ore is dissolved and leached by industrial grade hydrochloric acid (mass concentration 35%), and the added amount of hydrochloric acid is controlled so that the pH value of the leached solution is 3.5, and then the leached solution is press-filtered to obtain nickel chloride For the leach solution, barium chloride is added to the leach solution to remove sulfate radicals, and then filtered twice and then sent to P507 nickel soap for extraction and impurity removal to produce a nickel chloride solution with low impurity content;
[0034] The specific extraction process is: after mixing the P507 extractant and sulfonated kerosene at a ratio of 1:3, adding a NaOH solution with a mass concentration of 30% for saponification,...
Embodiment 2
[0041] Embodiment 2 step process is the same as embodiment 1, specifically:
[0042] The difference between step a and Example 1 is that the solution pH value after the control leaching is 3.8; in the extraction process, adding Ni ion concentration to the organic after saponification is that the nickel chloride solution of 80g / L produces nickel soap, The organic after nickel soap is mixed with the nickel chloride pre-extraction solution after removing sulfate radicals for extraction, and the loaded organic after extraction is extracted and regenerated with 5mol / L hydrochloric acid, and then re-saponified for reuse.
[0043] The difference between step b and Example 1 is that the concentration of the raw material nickel chloride solution is controlled at a nickel content of 45g / l, and the concentration of the sodium carbonate solution is controlled at a solute content of 150g / l; when the pH of the reaction solution reaches 8.3, stop adding Sodium carbonate solution, filter the ...
Embodiment 3
[0047] Embodiment 3 step process is the same as embodiment 1, specifically:
[0048] The difference between step a and Example 1 is that the solution pH value after the control leaching is 4.0; in the extraction process, adding Ni ion concentration to the organic after saponification is that the nickel chloride solution of 100g / L produces nickel soap, The organic after nickel soap is mixed with the nickel chloride pre-extraction solution after removing sulfate radicals for extraction, and the loaded organic after extraction is extracted and regenerated with 5.2mol / L hydrochloric acid, and then re-saponified for reuse.
[0049] The difference between step b and Example 1 is that the concentration of the raw material nickel chloride solution is controlled at a nickel content of 50g / l, and the concentration of the sodium carbonate solution is controlled at a solute content of 140g / l; when the pH of the reaction solution reaches 8.5, stop Add sodium carbonate solution, filter the ...
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