Simulation device and simulation method for repairing uranium-polluted underground water and recovering uranium
The technology of a simulation device and simulation method, which is applied in the field of repair and uranium recovery simulation devices, can solve the problems of low recovery efficiency, secondary pollution, impracticality, etc., and achieve the effects of increasing reaction rate, full reaction, and large reaction area
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Embodiment 1
[0040] In the model of polluted groundwater containing uranium 10mg / L, the layered thin iron material is used as the anode, the high-strength conductive carbon material is used as the cathode, and the light intensity is controlled at 51200Lux. After 2 hours of reaction, uranium-containing magnetite is formed, and the uranium in the solution The removal rate reached 85.92%; the uranium-containing magnetic iron tetroxide was placed in a muffle furnace, roasted at 650°C for 1h, cooled to room temperature, taken out, and stirred and leached with 30g / L dilute sulfuric acid for 1h, the recovery rate of uranium Reaching 81%, the dissolution rate of iron is only 0.34%.
Embodiment 2
[0042] In the model of polluted groundwater containing uranium 10mg / L, the layered thin iron material is used as the anode, the high-strength conductive carbon material is used as the cathode, and the light intensity is controlled to 44000Lux. After 2 hours of reaction, uranium-containing magnetite is formed, and the uranium in the solution The removal rate reached 84.21%; put the uranium-containing magnetic iron tetroxide in a muffle furnace, roast it at 700°C for 1h, take it out after cooling to room temperature, and use 30g / L dilute sulfuric acid to stir and leach for 1h. The recovery rate of uranium Reaching 83%, the dissolution rate of iron is only 0.32%.
Embodiment 3
[0044] In the polluted groundwater model with uranium content of 10 mg / L, layered thin iron material is used as the anode, high-strength conductive carbon material is used as the cathode, and the light intensity is controlled at 33500 Lux. After 2 hours of reaction, uranium-containing magnetite is formed, and the uranium in the solution The removal rate reached 88.68%; take the uranium-containing magnetic ferroferric oxide and place it in a muffle furnace, roast it at 700°C for 1h, take it out after cooling to room temperature, and use 20g / L dilute sulfuric acid to stir and leach for 1h. The recovery rate of uranium Reaching 82%, the dissolution rate of iron is only 0.27%.
[0045] See Table 1 for the changes in the indicators of the polluted water body before and after the treatment of the specific embodiments above.
[0046] serial number Light intensity (Lux) Initial U 6+ Concentration (mg / L)
[0047] In the process of treating uranium-contaminated water, th...
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