Recovery method of palladium in spent fuel element fission product
A fission product and recovery method technology, applied in the field of resource utilization and environmental protection, can solve the problems of poor decontamination ability of actinides, lanthanides and transition metals, difficult selective separation of palladium, multiple operations of secondary wastes, etc. Achieve the effect of easy engineering scale-up, strong applicability, and high recovery yield
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Embodiment 1
[0032] (a) After shearing 1.0g of spent fuel element, dissolve it in 180 mL of mixed acid consisting of hydrofluoric acid, nitric acid, and perchloric acid (volume ratio: 5:3:2) at 300°C, and then Adjust the price with hydrogen peroxide, concentrate and evaporate to dryness to obtain a solid particle sample;
[0033] (b) Redissolve the solid particle sample obtained in step a in 8.0 mol / L nitric acid solution, concentrate and evaporate to near dryness, then add 15 mL of 1.0 mol / L hydrochloric acid solution until completely dissolved to obtain the column sample solution ;
[0034] (c) The upper column sample solution obtained by step b is transferred to the balanced commercial strong acid ion exchange resin column for separation. The length of this commercial strong acid ion exchange resin column is 30 cm, and the radius is 1 cm. The flow rate of the effluent is controlled to be 0.5 mL / min, collect the sample effluent;
[0035] (d) the sample effluent obtained in step c is tr...
Embodiment 2
[0038] The implementation of this example is basically the same as that of Example 1, the main difference being that the heating and dissolving temperature in step a is adjusted to 200°C and 350°C respectively, the recovery yield of palladium and the decontamination factor of interfering elements obtained are the same as those of the implementation Compared with Example 1, there was no significant change.
Embodiment 3
[0040] The implementation of this example is basically the same as Example 1, the main difference is that the volume of the mixed acid in step a is adjusted to 250 mL and 360 mL respectively, the recovery yield of palladium obtained and the decontamination factor of interfering elements are the same as those of the implementation Compared with Example 1, there was no significant change.
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