Two-feeding-opening fully-loaded rare earth fractional extraction separation process method
A technology of two feed inlets and a process method is applied in the field of hydrochloric acid extractant to achieve the effects of improving the degree of greening, reducing the separation cost and increasing the concentration
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Embodiment 1
[0027] Fractional distillation extraction with full load at the second feed port ~ Nd / Sm ~ group separation of monazite rare earth ore and medium yttrium and europium rich ore
[0028] 1) Rare earth liquid
[0029] The first rare earth feed solution is an aqueous chloride solution of monazite rare earth ore, the rare earth concentration is 1.2 M, the pH value is 3, the molar fraction of light rare earth La to Nd is 0.95, and the molar fraction of medium and heavy rare earth Sm to Lu and Y is 0.05.
[0030] The second rare earth feed solution is a rare earth chloride aqueous solution of medium yttrium and europium-rich ore. The mole fraction is 0.45.
[0031] The molar ratio of feed amount of medium yttrium and europium-rich ore liquid to monazite rare earth ore liquid is 1:1.
[0032] 2) Rare earth extraction organic phase
[0033] The rare earth extraction organic phase is a kerosene solution of P507, and the volume percentage concentration of P507 is 36%; it is added to ...
Embodiment 2
[0048] Fractional distillation extraction with full load at the second feed port~Nd / Sm~Group separation of bastnaesite and medium yttrium-europium-enriched ore
[0049] 1) Rare earth liquid
[0050] The first rare earth feed solution is bastnaesite chloride aqueous solution, its rare earth concentration is 1.5 M, pH value is 4, the mole fraction of light rare earth La~Nd is 0.98, and the mole fraction of medium and heavy rare earth Sm~Lu and Y is 0.02.
[0051] The second rare earth feed solution is a rare earth chloride aqueous solution of medium yttrium and europium-rich ore. The mole fraction is 0.45.
[0052] The molar ratio of feed amount of middle yttrium and europium-rich ore liquid to bastnaesite feed liquid is 1:2.
[0053] 2) Rare earth extraction organic phase
[0054] The rare earth extraction organic phase is a kerosene solution of P507, and the volume percentage concentration of P507 is 35%; it is added to the fractionation extraction system in the form of li...
Embodiment 3
[0069] Separation of Terbium and Dysprosium by Fractional Distillation Extraction of Tb / Dy with Two Feed Inlets
[0070] 1) Rare earth liquid
[0071] The first rare earth feed liquid is an aqueous solution of terbium-dysprosium chloride, the rare earth concentration is 1.0 M, the pH value is 5, the mole fraction of terbium (Tb) is 0.60, and the mole fraction of dysprosium (Dy) is 0.40.
[0072] The second rare earth feed liquid is an aqueous solution of terbium-dysprosium chloride, the rare earth concentration is 1.0 M, the pH value is 3, the mole fraction of terbium (Tb) is 0.40, and the mole fraction of dysprosium (Dy) is 0.60.
[0073] The molar ratio of the feed amount of the second rare earth feed liquid to the first rare earth feed liquid is 1:1.
[0074] 2) Rare earth extraction organic phase
[0075] The organic phase of rare earth extraction is sulfonated kerosene solution of P507, and the concentration of P507 is 30% by volume; it is added to the fractionation ext...
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