Process for extracting rare earth element by non-saponifiable phosphorous mixing extractant
A technology of mixing extraction agents and rare earth elements, applied in the direction of improving process efficiency, etc., can solve the problems of large acid consumption, high residual acid in stripping liquid, environmental pollution, etc., and achieve the effect of reducing acid consumption and easy stripping
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Embodiment 1
[0033] 1000 grams of bastnaesite and monazite mixed rare earth ore (REO 50%) are roasted with sulfuric acid, soaked in water, neutralized and removed to obtain 11.5 liters of pure rare earth sulfate solution, the acidity is pH 4, and the main component is REO 40g .L, Fe2 2 o 3 / REO<0.05%) consumes 30ml of concentrated hydrochloric acid (about 33 grams) to produce samarium europium gadolinium enrichment or further extraction and separation.
[0034] The raffinate obtained (11.7 liters of rare earth sulfate solution containing lanthanum, cerium, praseodymium and neodymium 38.3g / l, Sm 2 o 3 / REO<0.003%) filter after being neutralized to PH4 with 95 grams of magnesia, filtrate adopts 1.5mol / l P2O4 complete extraction, 6mol / L hydrochloric acid back extraction, obtain containing lanthanum cerium praseodymium neodymium 267g / l rare earth chloride solution 1642ml ( Consumption of concentrated hydrochloric acid 1037ml, about 1141 grams), can produce lanthanum cerium praseodymium neody...
Embodiment 2
[0041]1000 grams of bastnaesite and monazite mixed rare earth ore (REO 50%) are roasted with sulfuric acid, soaked in water, neutralized and removed to obtain 12.5 liters of pure rare earth sulfate solution, the acidity is pH 4, and the rare earth concentration REO is 36.5 g / L, without adjusting acidity, directly use 70% non-saponifiable P204 (1.0mol / L) and 30% non-saponifiable P507 (1.0mol / L) mixed extractant for Nd / Sm extraction grouping, using 7-stage extraction, 13-stage washing, 8-stage stripping, compared: organic / material liquid / washing liquid is 0.25 / 1 / 0.014, and the washing liquid adopts a rare earth chloride solution containing samarium, europium, and gadolinium 215g / l and an acidity of 1.2mol / L (consumption concentrated Hydrochloric acid 111ml, about 122 grams), the concentration of rare earth in the washing section is 255g / l, the organic phase of loaded rare earth contains rare earth 18g / l, back extraction with 6mol / L hydrochloric acid, obtain containing REO 225g / l,...
Embodiment 3
[0046] 1000 grams of bastnaesite and monazite mixed rare earth ore were roasted with sulfuric acid, soaked in water, neutralized and removed to obtain a pure rare earth sulfate solution with an acidity of pH 4.5 and a REO concentration of 43g / L. A mixed extractant of 70% 1.2 mol / L non-saponifiable P204 and 30% 1.2 mol / L non-saponifiable P507 was used for fractional extraction and separation of cerium / praseodymium. The last stage of the stripping section enters 5.5mol / L hydrochloric acid to back-extract the organic phase loaded with rare earth, and the first-stage water phase of the back-extraction (retraction liquid REO 230g / l, 1.2mol / L, Nd 2 o 3 / REO 2 / REO2 o 3 / REO45%) ).
[0047] Compared with Comparative Example 3, this process does not need to add sulfuric acid to adjust the acidity of the feed liquid, and also saves a magnesium oxide neutralization and filtration process. One fractionation extraction can produce three marketable products, and the rare earth recovery ...
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