A method for purifying uranium from alkali slag leaching solution with multi-outlet design
A purification method and multi-export technology, applied in the field of hydrometallurgy, can solve the problems of reducing the concentration of uranium in purified wastewater, the influence of uranium purification effect, and reducing the amount of purified wastewater, so as to reduce the consumption of reagents, have strong practicability and good effect. Effect
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example 1
[0051]In an alkali slag leaching solution, the uranium concentration is 120g / L, the nitric acid concentration is 3.2mol / L, the total mass concentration of impurities is 80g / L, and the turbidity is 35ppm.
[0052] During the extraction process, the concentration of TBP in the organic phase is 30%, and the extraction flow ratio V O :V A The ratio is 1:0.87, the number of extraction stages is 5, the extraction temperature is 18°C, and the uranium concentration in the obtained loaded organic phase is 104.5g / L. The return ratio of the water phase is 50%, the export is increased in the fourth stage, and the concentration of uranium in the raffinate water phase is 4.1mg / L.
[0053] During the washing process, water is used as the detergent at the start, and after the back extraction liquid is prepared, the back extraction liquid is used as the detergent, and the washing flow ratio V O :V A The ratio is 15:1, the number of washing stages is 2, and the washing temperature is 18°C. T...
example 2
[0056] In an alkali slag leaching solution, the uranium concentration is 96g / L, the nitric acid concentration is 2.5mol / L, the total mass concentration of impurities is 58.2g / L, and the turbidity is 40ppm.
[0057] During the extraction process, the TBP concentration in the organic phase is 24%, and the extraction flow ratio V O :V A The ratio is 1:0.87, the number of extraction stages is 5, the extraction temperature is 22°C, and the uranium concentration in the obtained loaded organic phase is 83.6g / L. The return ratio of the water phase is 45%, the export is increased in the fourth stage, and the concentration of uranium in the raffinate water phase is 3.2mg / L.
[0058] During the washing process, 3mol / L nitric acid solution is used as the detergent for starting, and after the back extraction liquid is prepared, the back extraction liquid is used as the detergent, and the washing flow ratio V O :V A The concentration of uranium in the loaded organic phase after washing w...
example 3
[0061] In a certain alkali slag leaching solution, the uranium concentration is 132g / L, the nitric acid concentration is 3.5mol / L, the total mass concentration of impurities is 67.7g / L, and the turbidity is 32ppm.
[0062] During the extraction process, the concentration of TBP in the organic phase is 30%, and the extraction flow ratio V O :V A The ratio is 1:0.8, the number of extraction stages is 6, the extraction temperature is 15°C, and the uranium concentration in the obtained loaded organic phase is 105.6g / L. The return ratio of the water phase is 35%, the export is increased in the fourth stage, and the concentration of uranium in the raffinate water phase is 4.8mg / L.
[0063] During the washing process, 1mol / L nitric acid solution is used as the detergent at the start, and after the back extraction liquid is prepared, the back extraction liquid is used as the detergent, and the washing flow ratio V O :V A The concentration of uranium in the loaded organic phase afte...
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