Ore leaching method for ion-adsorbing type rare earth ore
A rare earth ore, adsorption-type technology, applied in the direction of improving process efficiency, can solve the problems of large amount of leaching aid and increased production cost, and achieve the effects of reducing dosage, promoting desorption, and reducing ammonia nitrogen pollution
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Embodiment 1
[0035] Take 300 g of dry Longnan ion-adsorption type rare earth ore with an ion-phase rare earth grade of 0.8‰, and put it into a leaching column with an inner diameter of 45 mm. First, 150ml of ammonium sulfate solution with a concentration of 0.20mol / L is used as the leaching agent solution for the first leaching, and the rare earth leachate is collected for the first time; The mixed solution with EDTA concentration of 0.05mol / L is leached for the second time. When the concentration of rare earth in the effluent of the leaching column is less than 0.1g / L, the liquid addition is stopped, and the second rare earth leachate is collected; the peristaltic pump controls the leaching process The flow rate of the medium addition liquid is 0.8ml / L. The two leaching solutions were combined to form a total of 297ml. The rare earth concentration in the rare earth leaching solution was 0.79g / L (calculated as REO), and the rare earth leaching rate was 98.1%.
Embodiment 2
[0037] Take 300 g of dry Longnan ion-adsorption type rare earth ore with an ion-phase rare earth grade of 0.8‰, and put it into a leaching column with an inner diameter of 45 mm. First, 90ml of magnesium sulfate solution with a concentration of 0.30mol / L is used as the leaching agent solution for the first leaching, and the first rare earth leaching solution is collected; then the concentration of the leaching agent potassium sulfate is 0.10mol / L, and the leaching aid The mixed solution with a tea saponin concentration of 0.03mol / L is leached for the second time, and when the concentration of rare earth in the effluent of the leaching column is less than 0.1g / L, stop adding liquid, and collect the second rare earth leachate; the peristaltic pump controls the leaching The flow rate of liquid addition during extraction is 0.8ml / L. The two leaching solutions were combined to form a total of 302ml. The rare earth concentration in the rare earth leaching solution was 0.78g / L (calcu...
Embodiment 3
[0039] Take 300 g of dry Longnan ion-adsorption type rare earth ore with an ion-phase rare earth grade of 1.6‰, and put it into a leaching column with an inner diameter of 45 mm. First, use 210ml leaching agent solution for the first leaching, the concentrations of magnesium sulfate and ammonium sulfate in the leaching agent solution are 0.05mol / L respectively, and the rare earth leaching solution is collected for the first time; then configure the leaching agent magnesium sulfate concentration to be 0.10mol / L, the leaching aid glycine concentration is the mixed solution of 0.15mol / L to carry out the second leaching, when the rare earth concentration in the leaching column effluent is less than 0.1g / L, stop adding liquid, collect and obtain the second rare earth leachate; The peristaltic pump controls the flow rate of liquid addition during the leaching process to be 0.8ml / L. The two leaching solutions were combined to form a total of 297ml. The rare earth concentration in th...
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