Process for extracting rare earth from phosphate concentrate
A phosphate concentrate and rare earth technology, which is applied in the extraction of rare earth elements and the whole process technology field, can solve the problems of unsatisfactory extraction and separation of impurity ions and low extraction efficiency, and achieve the goals of saving acid consumption, improving extraction efficiency and reducing impurities The effect of content
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Embodiment 1
[0034] Rare earth phosphorus concentrate P 2 o 5 36.09%, REO0.14%. Normal temperature hydrochloric acid decomposes once, the solid-to-liquid ratio is 1:3, the decomposition time is 1 hour, and the amount of hydrochloric acid by weight is 0.5 times the weight of ore. Suction filtration is carried out after the decomposition is completed, and the filter residue is washed with warm water at 50-60°C. The rare earth leaching rate is 0.1%, and the primary slag yield is 47%. The amount of nitric acid used for secondary slag decomposition is 0.8 times the ore weight, the solid-liquid ratio is 1:5, the decomposition time is 4.0 hours, and the decomposition temperature is 90°C. Take 400ml P350 and 600ml n-heptane, mix well, and prepare the extracted organic phase. A 100ml separatory funnel was used as a reactor for 8-stage countercurrent extraction, the flow ratio of the organic phase to the solid liquid was 1:2, the extraction mixing time was 5 minutes, and the extraction and clar...
Embodiment 2
[0036] Rare earth phosphorus concentrate P 2 o 5 36.09%, REO0.14%. The primary decomposition temperature of hydrochloric acid is 25°C, the solid-to-liquid ratio is 1:5, and the decomposition time is 3 hours. The amount of hydrochloric acid by weight is 0.8 times the weight of ore. Suction filtration is carried out after the decomposition is completed, and the filter residue is washed with warm water at 50-60°C. The rare earth leaching rate is 3.4%, and the primary slag yield is 32%. The amount of nitric acid used for secondary slag decomposition is 1.2 times the ore weight, the solid-liquid ratio is 1:3, the decomposition time is 2.0 hours, and the decomposition temperature is 60°C. Take 300ml P350 and 700ml n-heptane, mix well, and prepare the extracted organic phase. A 100ml separatory funnel was used as a reactor to carry out 6-stage countercurrent extraction, and the flow ratio of the organic phase to the feed liquid was 1:4. The extraction mixing time is 5min, and t...
Embodiment 3
[0038] Rare earth phosphorus concentrate P 2 o 5 36.09%, REO0.14%. The primary decomposition temperature of hydrochloric acid is 60°C, the solid-to-liquid ratio is 1:2, and the decomposition time is 4 hours. The amount of hydrochloric acid by weight is 1.5 times the weight of ore. Suction filtration is carried out after the decomposition is completed, and the filter residue is washed with warm water at 50-60°C. The rare earth leaching rate is 5.6%, and the primary slag yield is 28%. The amount of nitric acid used for secondary slag decomposition is 1.8 times the ore weight, the solid-liquid ratio is 1:4, the decomposition time is 1.0 hour, and the decomposition temperature is 15°C. Take 700ml P350 and 300ml kerosene, mix well, and prepare the extracted organic phase. A 100ml separatory funnel was used as a reactor to carry out 4-stage countercurrent extraction, and the flow ratio of the organic phase to the feed liquid was 4:1. The extraction mixing time is 5min, and the...
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