Method for enriching and recovering rare earth from phosphate rock containing rare earth
A rare earth enrichment and rare earth technology, applied in the direction of improving process efficiency, can solve the problems of difficult solid-liquid separation of slurry, and achieve the effects of easy solid-liquid separation, reduced dissolution loss, and easy control of process conditions
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Embodiment 1
[0030] Prepare the mass concentration of phosphoric acid (in P) with industrial phosphoric acid, industrial sulfuric acid and water 2 o 5 meter) 35%, sulfuric acid concentration (as SO 4 2- Calculate) the mixed acid of phosphoric acid and sulfuric acid of 10g / L, then take an appropriate amount of the mixed acid and the rare earth-containing phosphate rock powder containing 0.14% rare earth according to the liquid-solid volume and mass ratio of 5:1L / kg, and the reaction temperature is 30°C , the reaction time is 2h, and the mixed slurry-1 is obtained; the mixed slurry-1 undergoes solid-liquid separation to obtain the rare earth enriched slag and the leachate-1, and the rare earth content in the obtained rare earth enriched slag is 1%, and 95% of the rare earth is enriched in in the slag. The rare earth enriched slag is leached with nitric acid and then filtered to obtain leach solution-2 containing rare earth, and then the rare earth is recovered from the leach solution-2 by...
Embodiment 2
[0032] Add the leach solution-1 obtained in the above example 1 and an appropriate amount of sulfuric acid into the phosphoric acid regeneration stirring tank to mix and react to regenerate phosphoric acid. The amount of sulfuric acid added is 1 times the mole number of calcium in the leach solution-1 in terms of molar ratio, and the reaction temperature is 80°C , the reaction time is 1h, and the mixed slurry-2 is obtained; the obtained mixed slurry-2 is divided into two parts, one of which is returned to the regeneration stirring tank as the return slurry, and the rest is subjected to solid-liquid separation to obtain phosphoric acid solution and gypsum slag. The obtained phosphoric acid solution is added appropriate amount of water and industrial sulfuric acid adjustment composition, obtains containing phosphoric acid mass concentration (in P 2 o 5 meter) 35%, sulfuric acid concentration (as SO 4 2- Calculate) the mixed acid of phosphoric acid and sulfuric acid of 15g / L, t...
Embodiment 3
[0034] Add the leaching solution-1 obtained in the above-mentioned Example 1 and an appropriate amount of sulfuric acid into the phosphoric acid regeneration stirring tank, and add an appropriate amount of the mixed slurry-1 obtained in Example 2, and mix and react for a period of time to regenerate the phosphoric acid. The molar ratio is 1 times the molar number of calcium in the leach solution-1, the reaction temperature is 80°C, and the reaction time is 1h to obtain the mixed slurry-2; the obtained mixed slurry-2 is divided into two parts, and one part is returned to the In the regenerated stirring tank, the rest is subjected to solid-liquid separation to obtain phosphoric acid solution and gypsum slag. The obtained phosphoric acid solution is added appropriate amount of water and industrial sulfuric acid adjustment composition, obtains containing phosphoric acid mass concentration (in P 2 o 5 meter) 35%, sulfuric acid concentration (as SO 4 2- Calculate) the mixed acid ...
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