A method for electric-assisted enhanced leaching of uranium in low-grade uranium ore
An enhanced leaching and low-grade technology, applied in the field of uranium leaching, can solve problems such as hindering uranium leaching, and achieve the effect of increasing leaching rate and simple process flow
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0039] Take 20g uranium ore (0.008% uranium content) into the electric assisted leaching tank, use 60g / L sulfuric acid as the leaching agent, metal iron as the anode, graphite as the cathode, control the current intensity to 0.4A, and the solid-liquid ratio to 1:30. Air was introduced into the leaching solution, the concentration of oxygen in the leaching solution was 6 mg / l, the leaching time was 2 hours, the stirring speed was 150 r / min, the leaching rate of uranium at different leaching temperatures was shown in figure 2 . Under the same conditions, the uranium leaching rate of the electric assisted leaching example 1 is 23% higher than that of the direct acid leaching comparative example 1.
Embodiment 2
[0041] Take 20g of uranium ore (0.008% uranium content) into the electric assisted leaching tank, use 60g / L sulfuric acid as the leaching agent, metallic iron as the anode, and graphite as the cathode, control the current intensity to 0.4A, and the leaching temperature to 25°C. Into the air, the concentration of oxygen in the leaching solution is 8mg / l, the leaching time is 2h, the stirring speed is 150r / min, the leaching rate of uranium under different solid-liquid ratios is shown in image 3 . Under the same conditions, the uranium leaching rate of the electric assisted leaching example 2 is 21% higher than that of the direct acid leaching comparative example 2.
Embodiment 3
[0043] Take 25g of uranium ore (0.01% uranium content) into the electric assisted leaching tank, the metal iron is the anode, the graphite is the cathode, the control current intensity is 0.4A, the leaching temperature is 25°C, and air is passed into the leaching solution, and the oxygen in the leaching solution The concentration is 8mg / l, the leaching time is 2h, the solid-liquid ratio is 1:30, the stirring speed is 150r / min, the leaching rate of uranium under different sulfuric acid concentrations is shown in Figure 4 . Under the same conditions, the leaching rate of uranium in the electric assisted leaching example 3 is 40% higher than that in the direct acid leaching comparative example 3.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


