Method for directly preparing cerium fluoride by extraction and separation
A separation process, cerium fluoride technology, applied in chemical instruments and methods, fluoride preparation, inorganic chemistry, etc., can solve the difficult control of cerium fluoride particle size distribution, poor settling performance and filtration performance of cerium fluoride slurry, To deal with problems such as complex process, to achieve the effect of reducing the consumption of raw and auxiliary materials and production costs, controlling the particle size distribution of products, and uniform particle size distribution
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Embodiment 1
[0026] The hydrogen ion concentration of the rare earth sulfate solution is 0.2mol / L, the rare earth concentration is 0.1mol / LREO, the tetravalent cerium is 0.01mol / L, and the fluorine concentration is 0.01mol / L. It is obtained by mixing P507 and kerosene at a ratio of 1:2. The extraction system carries out the extraction of tetravalent cerium and fluorine, the number of extraction stages is 3, the flow ratio of P507 organic phase and feed liquid is controlled to be 0.2, and the organic phase loaded with tetravalent cerium and fluorine is obtained;
[0027] Sulfuric acid with a hydrogen ion concentration of 1mol / L is used as the washing solution, and the flow ratio of the organic phase to the washing solution is 2:1 for two-stage washing;
[0028] Back-extraction was carried out at 20°C, and the back-extraction liquid was 2 o 2 The hydrochloric acid mixed solution, the hydrogen ion concentration is 0.5mol / L, the amount of hydrogen peroxide is twice the theoretical amount, the...
Embodiment 2
[0030] The hydrogen ion concentration of the rare earth sulfate solution is 0.5mol / L, the rare earth concentration is 0.06mol / LREO, the tetravalent cerium is 0.05mol / L, and the fluorine concentration is 0.1mol / L. It is obtained by mixing P507 and kerosene at a ratio of 0.3:1 The extraction system carries out the extraction of tetravalent cerium and fluorine, the number of extraction stages is 10, and the flow ratio of P507 organic phase and feed liquid is controlled to be 1:1 to obtain an organic phase loaded with tetravalent cerium and fluorine;
[0031] Use a hydrogen ion concentration of 2mol / L nitric acid washing solution with a flow ratio of 3:1 for the first-stage washing;
[0032] Back-extraction was carried out at 65°C, and the back-extraction solution was 2 o 2 A mixed solution of 2.0mol / L hydrochloric acid and 0.30mol / L hydrofluoric acid, the amount of hydrogen peroxide is 1.5 times of the theoretical amount, and the sum of the molar amounts of fluorine in the strip...
Embodiment 3
[0034] The hydrogen ion concentration of rare earth sulfate solution is 0.5mol / L, the concentration of rare earth oxide REO is 0.05mol / L, among which the concentration of tetravalent cerium is 0.01mol / L, and the concentration of fluorine is 0.01mol / L. The ratio of P507 and kerosene is 0.2:1 The extraction system obtained by mixing is extracted with tetravalent cerium and fluorine, the extraction stage is 1, and the flow ratio of P507 organic phase and feed liquid is controlled to be 1.5:1, so as to obtain an organic phase loaded with tetravalent cerium and fluorine;
[0035] Using sulfuric acid with a hydrogen ion concentration of 3mol / L as the washing solution, the flow ratio of the organic phase to the washing solution is 3 for 8-stage washing;
[0036] Back-extraction was carried out at 25°C, and the back-extraction solution was 2 o 2hydrochloric acid solution, the hydrogen ion concentration is 2.0mol / L, the amount of hydrogen peroxide is 1.5 times of the theoretical amoun...
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