Method for extracting and separating high-purity dysprosium oxide and terbium oxide from terbium-dysprosium rare earth enrichment matters
A rare earth enrichment and terbium oxide technology, which is applied in the field of rare earth separation, can solve the problems of high commissioning cost, high acid-base consumption, and large amount of terbium element pressing, so as to reduce commissioning costs, save one-time investment, and reduce investment costs. Effect
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Embodiment 1
[0021] Implementation example 1: with raw materials Ⅰ As the feed solution of terbium-dysprosium enrichment, ① firstly pre-group in molar fraction of 0.55:0.45, extract part of the aqueous phase La~GdTbDy material to make rare earth soap, and then separate into two intermediate feed liquids, La~GdTbDy and DyHoY~; ② Middle The feed liquid directly enters the series separation process linkage, and after drawing out part of the aqueous phase La~GdTb material to make rare earth soap, it is then separated into: La~GdTb, HoY~ two pure enrichments and high-purity Dy products; ③ The separated intermediate products La~GdTb feed liquid, and then enter the La~Gd / / Tb two-outlet separation process to separate into La~Gd pure enrichment and high-purity Tb products. If the process uses high-grade pure hydrochloric acid as wash-back acid, the precipitant is purified Oxalic acid can produce fluorescent grade high-purity terbium oxide products (see the process flow figure 1 , figure 2 ).
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Embodiment 2
[0028] Example 2: Using raw material II as the feed liquid of the terbium-dysprosium enrichment, 1. firstly pre-group by molar fraction of 0.6:0.4, draw out part of the aqueous phase ~SmEuGdDy material to make rare earth soap, and then separate it into ~SmEuGdTbDy and DyHo~LuY two The intermediate feed liquid; ②The intermediate feed liquid directly enters the series separation process linkage, and part of the water phase ~SmEuGdTb material is extracted to make rare earth soap, and then separated into: ~SmEuGdTb, HoY~ two pure enrichments and high-purity Dy products; ③Separation The intermediate product ~SmEuGdTb feed liquid, and then enter the ~SmEuGd / / Tb two-outlet separation process to separate into ~SmEuGd pure enrichment and high-purity Tb products. Refined oxalic acid can produce fluorescent-grade high-purity terbium oxide products (see the process flow figure 1 , figure 2 ).
[0029] The organic phase consists of extractant: bis(2-ethylhexyl)2-ethylhexylphosphoric aci...
Embodiment 3
[0035] Example 3: Using the raw material III as the feed liquid of the terbium-dysprosium enrichment, ① firstly pre-group by molar fraction of 0.5:0.5, and extract part of the aqueous phase La~GdDy materials to prepare rare earth soap, and then separate into La ~GdTbDy and DyHo~LuY two intermediate feed liquids; ②The intermediate feed liquid directly enters the series separation process, and part of the aqueous phase La~GdTb material is extracted to make rare earth soap, and then separated into: La~GdTb, Ho~LuY two pure rich Aggregates and high-purity Dy products; ③ separated intermediate products La ~GdTb feed liquid, and then enter the La~Gd / / Tb two-outlet separation process to separate into La~Gd pure concentrates and high-purity Tb products. If the process uses high-grade pure hydrochloric acid as the washing and reverse acid, the precipitating agent uses refined oxalic acid It can produce fluorescent grade high-purity terbium oxide products (see the process flow figure...
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