Technique for extracting and separating rare earth elements from non-saponification system
A rare earth element, non-saponification technology, applied in the field of extraction and separation of rare earth elements, can solve the problems of large investment in equipment extractant, difficult stripping of medium and heavy rare earths, and high residual acid in stripping liquid, so as to save the cost of three wastes treatment, easy to control, The effect of reducing acid consumption and cost
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Embodiment 1
[0022] Bastnaesite and monazite mixed rare earth ore (REO 50%) undergoes sulfuric acid roasting, water immersion, neutralization and impurity removal to obtain a pure sulfuric acid rare earth solution with an acidity of pH 4 and main components of REO 40g / L, Fe 2 2 o 3 The content is less than 0.01%.
[0023] The obtained lanthanum cerium praseodymium neodymium raffinate (Sm 2 o 3 content is less than 0.005%), neutralized to PH4 with magnesium oxide, fully extracted with 1.5mol / l non-saponifiable P204, back-extracted with 5.5N hydrochloric acid, to obtain a rare earth chloride solution containing 267g / l of lanthanum, cerium, praseodymium and neodymium, which is produced by concentrated crystallization Lanthanum cerium praseodymium neodymium rare earth chloride products, of which REO>45%, Sm 2 o 3 The content is less than 0.005%. From the sulfuric acid rare earth solution to the product, the total rare earth yield is 98.2%.
Embodiment 2
[0025]Bastnaesite (REO 60%) undergoes sulfuric acid roasting, water immersion, neutralization and impurity removal to obtain a pure rare earth sulfate solution with an acidity of pH 4.5 and a rare earth concentration of REO 36g / L. Carry out Nd / Sm extraction and grouping, use 10-stage extraction, 18-stage washing, and 9-stage back-extraction. The washing solution is a rare earth chloride solution containing 255g / l of samarium, europium, and gadolinium, and an acidity of 0.3N. The rare earth-loaded organic phase contains 12g / l of rare earth , back-extracted with 5.2N hydrochloric acid to obtain a samarium-europium-gadolinium rare-earth chloride solution containing REO 255g / l and an acidity of 0.3N. After precipitation and oxalic acid precipitation, burning produces samarium-europium-gadolinium enrichment or further extraction and separation of samarium, europium, and europium. Gadolinium single rare earth products.
[0026] The obtained raffinate containing lanthanum, cerium, pr...
Embodiment 3
[0028] Front part process is the same as embodiment 2
[0029] The obtained lanthanum, cerium, praseodymium and neodymium raffinate is neutralized to pH4 with magnesium oxide, then adopts the mixed extractant of 90% 1.5mol / L non-saponification P204 and 10% 1.5mol / L non-saponification C272 (with No. diluted with solvent naphtha) for cerium / praseodymium fractionation extraction grouping. The lotion is stripped with rare earth chloride containing praseodymium and neodymium (REO 258g / L), and the loaded rare earth organic phase is stripped with 6.0N hydrochloric acid; after 23 stages of extraction, 32 stages of washing, and 6 stages of stripping to obtain praseodymium and neodymium chloride (CeO 2 The content is less than 0.05%); the raffinate is neutralized to PH4.5 with magnesium oxide, lanthanum cerium is extracted with 1.5mol / L unsaponified P204, back-extracted with 5.3N hydrochloric acid, and the obtained lanthanum cerium chloride solution is concentrated and crystallized to p...
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