Method for separating valuable components of monazite slags
A separation method and technology of stone slag, applied in the field of separation of valuable components of solitary stone slag, can solve problems such as unfavorable environmental protection management, environmental hazards, and neglected recycling
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Embodiment 1
[0013] A method for separating valuable components of monazite slag, comprising the following steps:
[0014] (1) Acid leaching: According to the ratio of monazia slag (㎏):acid (L)=1:1~15, add monazia slag to the sulfuric acid solution with a concentration of 0.25mol / L~0.5mol / L, and heat to 40 ℃~100℃, stir for 5 hours to 8 hours, cool and stand for clarification for 4 hours to 8 hours, siphon the supernatant to obtain a solution containing uranium, thorium, and rare earth valuable elements;
[0015] In this example, according to the ratio of solitary slag (㎏): acid (L) = 1:10, the solitary slag (H 2 O: 30.80%, ThO 2 ﹪: 24.2﹪, REO﹪: 9.65﹪, U﹪: 0.77﹪) into the reaction kettle filled with sulfuric acid solution with a concentration of 0.25mol / L, heated to 55°C, stirred for 5 hours, cooled and clarified until the supernatant was clear , the standing time is 5h, siphon the supernatant to the storage tank, and leave the solid phase in the reactor.
[0016] (2) Pressure filtration...
Embodiment 2
[0023] In order to improve the recovery rate of valuable elements uranium, thorium and rare earth, the present invention carries out secondary acid leaching after step ⑴, according to the ratio of monazite slag (㎏):acid (L)=1:1~3, the concentration is 0.25 Add mol / L~0.5mol / L sulfuric acid solution into the slurry after siphoning supernatant, heat to 40℃~100℃, stir for 5 hours to 8 hours, cool and stand for clarification for 4 hours to 8 hours, siphon up The supernatant liquid obtained in step (1) is combined with the supernatant liquid to obtain a solution containing uranium, thorium, and rare earth valuable elements.
[0024] In this embodiment, after step ⑴, according to the ratio of monazia slag (㎏):acid (L)=1:2, a sulfuric acid solution with a concentration of 0.25mol / is added to the slurry after siphoning the supernatant, and heated to Stir at 60°C for 5 hours, cool and stand for clarification for 6 hours, siphon the supernatant and combine it with the supernatant obtaine...
Embodiment 3
[0030] In step (1) of this embodiment, according to the ratio of monazia slag (㎏): acid (L) = 1:12, monazia slag is added to the reaction kettle filled with sulfuric acid solution with a concentration of 0.25mol / L, and heated to 60 ℃, stirring for 6 hours, cooling and standing still to clarify until the supernatant is clear, standing time is 6h, siphon the supernatant into the storage tank, and keep the solid phase in the reaction kettle.
[0031] In order to improve the recovery rate of valuable elements uranium, thorium and rare earth, the present invention carries out secondary acid leaching after step (1), according to the ratio of monazite slag (㎏):acid (L)=1:1.5, the concentration is 0.35 mol / L sulfuric acid solution was added to the slurry after the siphon supernatant, heated to 80°C, stirred for 5 hours, cooled and left to clarify for 6 hours, the siphon supernatant was combined with the supernatant obtained in step (1) to obtain a mixture containing uranium, The solut...
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