Preparation method of low-thorium lutetium oxide
A technology of lutetium oxide and lutetium chloride, applied in chemical instruments and methods, inorganic chemistry, rare earth metal compounds, etc., can solve the problems of incomplete separation of rare earth and thorium, huge investment in equipment, difficulty in continuous production, etc., to achieve stratification Good, good separation effect, short series effect
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example 1
[0016] The lutetium chloride feed solution separated by extraction with P507 and other extractants has a rare earth concentration of 1.1mol / L and a thorium content of 56μg / ml. After the first countercurrent extraction of the 6-stage N235 extraction system, the concentration of N235 is 1.1mol / L, the diluent is kerosene, and the flow ratio used is extractant N235: lutetium chloride feed liquid=5: 1 (volume ratio), and the thorium chloride content in the lutetium chloride in the raffinate that obtains is reduced to 6.5 μ g / ml, the organic phase of the extracted thorium is back-extracted with 0.5mol / L sodium hydroxide and then recycled; The concentration of lutetium chloride is 0.6mol / L, and diluent is kerosene, and the flow ratio used is the kerosene solution of organic phase naphthenic acid: lutetium chloride feed liquid=3: 1 (volume ratio), in the raffinate lutetium chloride that obtains The thorium content is reduced to less than 0.1 μg / ml, and the concentration of lutetium ...
example 2
[0018] The lutetium chloride feed solution extracted and separated by extraction agents such as P507 has a rare earth concentration of 1.06mol / L and a thorium content of 356μg / ml. After the first countercurrent extraction of the 10-stage N235 extraction system, the concentration of N235 is 1.0 mol / L, the diluent is kerosene, and the flow ratio used is extractant N235: lutetium chloride feed liquid=8: 1 (volume ratio), and the thorium content in the raffinate lutetium chloride that obtains is reduced to 21.5 μ g / ml , the organic phase of the extracted thorium is back-extracted with 0.5mol / L sodium carbonate and then recycled; It is 0.55mol / L, diluent is kerosene, and used flow ratio is the kerosene solution of organic phase naphthenic acid: lutetium chloride feed liquid=4: 1 (volume ratio), the thorium in the raffinate lutetium chloride obtained The content is reduced to less than 0.1μg / ml, and the lutetium chloride is 0.95mol / L; the organic phase of the thorium extraction is s...
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