A method for extracting and separating high-purity dysprosium oxide and terbium oxide from terbium dysprosium rare earth enrichment
A rare earth enrichment and terbium oxide technology, applied in the field of rare earth separation, can solve the problems of high acid-base consumption, large debugging cost, large amount of terbium element pressing groove, etc., saving one-time investment, reducing debugging cost, and reducing investment cost Effect
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Embodiment 1
[0021] Implementation Example 1: Using raw material I as the feed liquid of terbium-dysprosium enrichment, ① first pre-grouping according to the molar fraction of 0.55:0.45, and drawing out part of the aqueous phase La~GdTbDy material to make rare earth soap, and then separating into La~GdTbDy and DyHoY~ An intermediate feed liquid; ②The intermediate feed liquid directly enters the series separation process linkage, leads out part of the aqueous phase La~GdTb material to make rare earth soap, and then separates into: La~GdTb, HoY~ two pure enrichments and high-purity Dy products ; ③The separated intermediate product La~GdTb feed liquid enters the La~Gd / / Tb two-outlet separation process to be separated into La~Gd pure enrichment and high-purity Tb products. For acid reflux, the precipitant uses refined oxalic acid to produce fluorescent grade high-purity terbium oxide products (see process flow figure 1 , figure 2 ).
[0022] The organic phase is composed of extractant: bis(...
Embodiment 2
[0028] Implementation Example 2: Using raw material II as the feed liquid of the terbium-dysprosium enrichment, ①first pre-grouping according to the molar fraction of 0.6:0.4, and drawing out part of the water phase~SmEuGdDy material to make rare earth soap, and separating into~SmEuGdTbDy and DyHo~LuY Intermediate feed liquid; ②The intermediate feed liquid directly enters the series separation process linkage, and after drawing out part of the water phase ~SmEuGdTb material to make rare earth soap, it is then separated into: ~SmEuGdTb, HoY~ two pure enrichments and high-purity Dy products; ③Separation The intermediate product ~SmEuGdTb feed liquid, then enters the ~SmEuGd / / Tb two-exit separation process to separate into ~SmEuGd pure enrichment and high-purity Tb products. If the process uses high-grade pure hydrochloric acid for acid washing, the precipitant Refined oxalic acid can produce fluorescent grade high-purity terbium oxide products (see process flow figure 1 , figu...
Embodiment 3
[0035] Implementation Example 3: Using raw material III as the feed liquid of terbium-dysprosium enrichment, ① first pre-grouping according to the molar fraction of 0.5:0.5, drawing out part of the aqueous phase La~GdDy material to make rare earth soap, and separating into La~GdTbDy and DyHo~LuY Two intermediate feed liquids; ②The intermediate feed liquid directly enters the series separation process, and after drawing out part of the aqueous phase La~GdTb material to make rare earth soap, it is then separated into two pure enrichments of La~GdTb and Ho~LuY and high-purity Dy products; ③The separated intermediate product La~GdTb feed liquid enters the La~Gd / / Tb two-exit separation process to separate into La~Gd pure enrichment and high-purity Tb products. If the process uses superior pure hydrochloric acid to make Fluorescence-grade high-purity terbium oxide products can be produced by using refined oxalic acid as precipitant (see process flow figure 1 , figure 2 ).
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