Device for removing iron from iron-containing solution of hydrometallurgy
A hydrometallurgical and solution technology, applied in the direction of improving process efficiency, can solve the problems of large consumption of reducing agent and oxidant, and achieve the effect of easy solid-liquid separation, improving recovery rate and reducing entrainment
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0028] use as figure 1 For the device shown, the concentration of ferric iron in the reactor is lower than 1g / L, and the pH of the solution in the reactor is controlled at 15g / L of ferric iron in the iron-containing solution after pressurized oxidation of a gold pressurized pre-oxidation project. =3~4, temperature 70°C, sulfuric acid 10g / L, using 4 goethite iron removal tanks (reactors), reaction time 2 hours, the concentration of ferric iron in the solution after iron removal is about 0.07g / L, except The iron rate is about 99%, and the underflow concentration of the thickener is 40%.
Embodiment 2
[0030] use as figure 1 For the device shown, a certain project contains 11g / L of ferric iron in copper solution, the concentration of ferric iron in the reactor is controlled to be lower than 1g / L, and the pH of the solution in the reactor is controlled to be 3~4, the temperature is 80°C, sulfuric acid 5g / L, using 3 goethite iron removal tanks (reactors), the reaction time is 1.5 hours, the concentration of ferric iron in the solution after iron removal is about 0.05g / L, the iron removal rate is about 99%, and the underflow concentration of the thickener 36%.
Embodiment 3
[0032] use as figure 1 For the device shown in the laboratory, for a certain iron-containing solution 6g / L, the concentration of ferric iron in the reactor is controlled to be lower than 1g / L, and the pH of the solution in the reactor is controlled to be 3-4, the temperature is 65°C, sulfuric acid 2g / L, using goethite iron removal tank (reactor), the reaction time is 2.5 hours, the concentration of ferric iron in the solution after iron removal is about 0.3g / L, the iron removal rate is about 95%, the bottom flow of the solid-liquid separation thickener Concentration 35%.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
