Ionic liquid extractant for plutonium recovery and method for extracting and separating plutonium from plutonium-containing waste liquid
An ionic liquid and extractant technology, applied in the field of radioactive waste liquid treatment, can solve problems such as toxicity, achieve good distribution rate, reduce the generation of secondary waste, and save economic costs.
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Embodiment 1
[0033] Add 100 mL of 1 mol / L nitric acid solution to 10 g of plutonium-contaminated soil, stir and rinse at room temperature for 6 hours, and collect the supernatant as the plutonium-containing waste liquid after solid-liquid separation. ) analyze the plutonium-239 content in the waste liquid; calculate the hydrogen ion concentration after measuring the pH of the waste liquid, add concentrated nitric acid to adjust the nitric acid concentration of the waste liquid system to be 6 mol / L, then add 3 mL of 30% hydrogen peroxide, and place it for 2h to remove excess hydrogen peroxide by heating; After cooling, take 20 mL of plutonium-containing waste liquid into a 100 mL plastic centrifuge tube, and then add 16 mL [C 6 mim]NTf 2 The ionic liquid and 4 mL of tributyl phosphate were shaken and mixed at room temperature for 30 minutes and then left to stand for stratification. The ionic liquid and waste liquid were collected separately, and 16 mL of [C 6 mim]NTf 2 The extraction wit...
Embodiment 2
[0043] Same as Example 1, the difference is that the ionic liquid extractant is: 15 mL [C 8 mim][PF 6 ], 2 mL of tributyl phosphate and 1 mL of thiopheneformyl trifluoroacetone; the back extraction agent was 0.1 mol / L oxalic acid.
[0044] Through detection, E=93.31%, E'=94.09%.
[0045] The repeated extraction effect of the ionic liquid extractant after stripping was tested: the ionic liquid after stripping was taken, and the waste liquid was extracted according to the same operation steps, and the extraction rate of plutonium-239 was 92.38%.
[0046] Achieved effect: the recovery rate of plutonium-239 is 87.80%, the ionic liquid can be reused after stripping, and no secondary waste is produced.
Embodiment 3
[0048] Same as Example 1, the difference is that the ionic liquid extractant is: 20 mL of component A and 4 mL of component B, wherein component A includes 10 mL [C 4 mim][NTf 2 ] and 10mL [C 6 mim][PF 6 ]; Component B is thiopheneformyl trifluoroacetone.
[0049] Through detection, E=94.02%, E'=92.71%.
[0050] The repeated extraction effect of the ionic liquid extractant after stripping was tested: the ionic liquid after stripping was taken, and the waste liquid was extracted according to the same operation steps, and the extraction rate of plutonium-239 was 92.23%.
[0051] Achieved effect: the recovery rate of plutonium-239 is 87.17%, the ionic liquid can be reused after stripping, and no secondary waste is produced.
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