Process for extracting rare earth element by non-saponifiable phosphorous mixing extractant
A technology of mixing extractants and rare earth elements, applied in the direction of improving process efficiency, can solve the problems of high nitric acid concentration, large acid consumption and high production cost, and achieve the advantages of improving stripping efficiency, improving production capacity and reducing acid consumption. Effect
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Embodiment 1
[0034] 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, Fe<0.05g / L, P<0.005g / L, ThO2<0.001g / L, directly use 60% non-saponifiable P204 (1.0mol / L) and 40% non-saponifiable P507 (1.0mol / L) Nd / Sm extraction grouping with the mixed extraction agent, using 7-stage extraction, 13-stage washing, 8-stage back extraction, compared: organic / material liquid / washing liquid is 0.25 / 1 / 0.015, and the washing liquid is 210g containing samarium, europium and gadolinium / l, acidity 1.5N rare earth chloride back-extraction liquid (consumption of concentrated hydrochloric acid 110ml, about 121 grams), the rare earth concentration in the washing section is 245g / l, and the loaded rare earth organic phase contains rare earth 18g / l, back-extracted with 6N hydrochloric acid to obtain Containing...
Embodiment 2
[0042] 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 rare earth chloride solution containing samarium, europium and gadolinium 215g / l, acidity 1.2N (consumption of concentrated hydrochloric acid 111ml , about 122 grams), the concentration of rare earths in the washing section is 255g / l, and the organic phase of loaded rare earths contains 18g / l of rare earths, and back-extracted with 6N hydrochloric acid to obtain 225g / l of REO and an a...
Embodiment 3
[0047] 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 5.5N hydrochloric acid to strip the rare earth-loaded organic phase, and the first stage of stripping the aqueous phase (the stripping liquid REO 230g / l, 1.2N, Nd2O3 / REO45%) through concentrated crystallization .
[0048] 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 rate is h...
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