Method for extracting and separating cerium, fluorine and phosphorus from sulfuric acid leaching solution of Baotou rare earth mine
A technology of Baotou rare earth and leaching liquid, applied in the field of separation, can solve the problem of high extraction cost, and achieve the effect of continuous process flow, good effect and good physical phenomenon.
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Embodiment 1
[0039] Using Baotou rare earth ore oxidative roasting-sulfuric acid leaching solution as the raw material solution, the raw material solution contains 15.5g / L CeO 2 , CeO 2 / REO (REO is the total content of rare earth oxides) is 47% (mass percentage, the same below), contains 3g / L of F, 0.56g / L of P, and the acidity of the feed liquid is 1.5mol / LH 2 SO 4 . Extract the above feed liquid with the extract at room temperature, the concentration of the washing liquid is 0.5mol / L sulfuric acid, the flow ratio of the organic phase of the extract, the feed liquid and the washing liquid is 1:1:0.2, and the number of stages in the extraction section is 2 , the number of stages of the washing section is 1, and the equilibrium time is 1min. The extract is prepared by diluting the extractant Cyanex923 with the diluent n-heptane, and the concentration of the extractant Cyanex923 in the diluent is 10%. After the extraction, the loaded organic phase containing cerium (IV), fluorine and pho...
Embodiment 2
[0041] Using Baotou rare earth ore oxidative roasting-sulfuric acid leaching solution as the raw material solution, the raw material solution contains 26.8g / L CeO 2 , CeO 2 / REO (REO is the total content of rare earth oxides) is 53%, contains 5g / L of F, 4.35g / L of P, and the acidity of the feed liquid is 2mol / LH 2 SO 4 . Extract the above feed liquid with the extract at room temperature, the concentration of the washing liquid is sulfuric acid of 3mol / L, the flow ratio of the organic phase of the extract, the feed liquid and the washing liquid is 4:1:1, and the number of stages in the extraction section is 15. The number of stages in the washing section is 10, and the equilibration time is 15 minutes. The extract is prepared by diluting the extractant Cyanex923 with diluent kerosene, and the concentration of the extractant Cyanex923 in the diluent is 20%. The loaded organic phase containing cerium (IV), fluorine and phosphorus obtained after extraction is back-extracted wit...
Embodiment 3
[0043] Using Baotou rare earth ore oxidative roasting-sulfuric acid leaching solution as the raw material solution, the raw material solution contains 20.3g / L CeO 2 , CeO 2 / REO (REO is the total content of rare earth oxides) is 49%, contains 4.48g / L of F, 2.56g / L of P, and the acidity of the feed liquid is 2.5mol / LH 2 SO 4 . Extract the above-mentioned feed liquid with the extraction liquid at room temperature, the concentration of the washing liquid is sulfuric acid of 1.5mol / L, the flow ratio of the organic phase of the extract liquid, the feed liquid and the washing liquid is 2:1:0.6, and the number of stages in the extraction section is 8 , the number of stages of the washing section is 6, and the equilibrium time is 8min. The extract is prepared by diluting the extractant Cyanex923 with an alkane with 13 carbon atoms in the diluent. The concentration of the extractant Cyanex923 in the diluent is 30 %. The loaded organic phase containing cerium (IV), fluorine and phos...
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