Continuous ion exchange process integrated with membrane separation for recovering uranium
a technology of continuous ion exchange and membrane separation, which is applied in the direction of transuranic element compounds, chemistry apparatus and processes, inorganic chemistry, etc., can solve the problems of loss of separation efficiency, and achieve the effect of reducing the concentration of competing anions
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[0005]The invention includes a system and method for recovering uranium from a pregnant liquor solution, (“PLS”). The source of the PLS is not particularly limited but is typically produced by heap leaching, in-situ leaching, vat leaching or pressure leaching of carbonate-containing uranium ores. In one embodiment, the leach ores reside in a lixiviation tank from which the PLS is drawn. The PLS comprises an alkaline solution preferably having a pH of at least 9 and more preferably at least 10; and further includes uranium, bicarbonate, carbonate, sulfate and chloride anions along with their counter cations and corresponding salts. Even though the concentration of these anions is dynamic, they are preferably maintained within the following ranges: carbonate: 10-60 g / L; bicarbonate: 1-20 g / L; chloride: 0 to 10 g / L; sulfate: 0-25 g / L. While the tetravalent uranyl tricarbonate complex anion UO2(CO3)34−− predominates, a divalent ion UO2(CO3)22− ·2H2O may exist at low carbonate concentrat...
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