Method for extracting rubidium salt and cesium salt
A technology for cesium salts and rubidium salts, which is applied in the field of extracting rubidium salts and cesium salts, can solve the problems that industrialization and semi-industrialization are far away, complicated in steps, waste of manpower, material resources, financial resources, time, etc. The extraction method is simple and the effect of good application prospects
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Embodiment 1
[0032] Adjust the pH of high-salinity solutions with sodium, potassium, rubidium, and cesium ions of 120g / L, 60g / L, 10g / L, and 1g / L to 12, and use t-BAMBP (t- The ratio of BAMBP and sulfonated kerosene is 1:3) to extract the alkalized raw material solution, the flow ratio of the organic phase to the aqueous phase is 3:1, the contact time of the two phases is controlled to be 5min, and the countercurrent series is 3 to obtain the loaded rubidium , the organic phase of cesium ions and the raffinate aqueous phase; the loaded organic phase is washed with 0.01mol / L sulfuric acid solution in countercurrent 5 stages, respectively using 0.5mol / L and 2mol / L sulfuric acid, the organic phase and the aqueous phase flow ratio Carry out 2-stage back extraction for 60:1, obtain 296g / L rubidium sulfate solution and 26.5g / L cesium sulfate solution, the blank organic phase is recycled.
Embodiment 2
[0034] Adjust the pH of high-salinity solutions with sodium, potassium, rubidium, and cesium ions of 90g / L, 10g / L, 25g / L, and 25g / L to 13, and use t-BAMBP (t- The ratio of BAMBP and sulfonated kerosene is 1:1) to extract the alkalized raw material solution, the flow ratio of the organic phase to the aqueous phase is 2:1, the contact time of the two phases is controlled to be 10min, and the countercurrent series is 4 to obtain the loaded rubidium , the organic phase of cesium ions and the raffinate aqueous phase; the loaded organic phase is washed with 0.01mol / L hydrochloric acid solution in countercurrent three stages, and the contents of rubidium chloride, potassium chloride and sodium chloride are respectively 325g / L, 1.8 g / L and 0.7g / L stripping solution, the yield of rubidium chloride was 96.2%, and the purity was 99.2%; further, 2mol / L hydrochloric acid was used, and the flow ratio of organic phase to aqueous phase was 20:1 for two-stage reaction Extraction, to obtain rub...
Embodiment 3
[0036] Adjust the pH of high-salinity media with sodium, potassium, rubidium, and cesium ions at 50g / L, 50g / L, 50g / L, and 50g / L to 13, and use t-BAMBP (t- The ratio of BAMBP and sulfonated kerosene is 1:1) to extract the alkalized raw material liquid, the flow ratio of the organic phase to the aqueous phase is 4:1, the contact time of the two phases is controlled to be 0.5min, and the countercurrent series is 5, and the load The organic phase of rubidium and cesium ions and the raffinate aqueous phase; the loaded organic phase is washed with 0.02mol / L sodium hydroxide solution and water respectively in countercurrent 8 stages, and the organic phase is washed with 1mol / L and 4mol / L nitric acid respectively. The 3-stage back-extraction was carried out at a ratio of 10:1 to the aqueous phase to obtain a 190g / L rubidium nitrate solution and a 169g / L cesium nitrate solution, and the blank organic phase was recycled.
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