Method for selectively separating chromium and ferrum in sulfate solution
The technology of a sulfuric acid system and a separation method is applied in the direction of improving the process efficiency, etc., and can solve the problems such as the failure to realize the resource utilization of valuable metals, the sensitivity of the addition amount of oxalic acid and temperature factors, and the large neutralization load of the initial solution, and achieve the separation effect. Ideal, significant economic benefit, low cost effect
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Embodiment 1
[0029] The content of Cr in the mixed solution of chromium and iron in the sulfuric acid system is 6.0 g / L, the content of Fe is 3.0 g / L, the reducing agent is sodium sulfite, and the sodium sulfite solution with a concentration of 20% and the mixed solution of chromium and iron are added dropwise at a ratio of 1:10. Add an appropriate amount of NaOH solution to adjust the pH of the solution to 2.0, add sodium phosphate according to the molar ratio of phosphate and chromium ions of 0.4, keep it warm at 90 °C for 60 min, control the stirring line speed at 200 m / min during the process, and filter to obtain chromium phosphate Chromium hydroxide composite precipitate, the concentrations of chromium and iron in the filtrate were 0.086 g / L and 2.91 g / L respectively, the recovery rate of chromium was 98.53%, the recovery rate of iron was 98.58%, and the separation coefficient of ferrochromium was 67.7.
Embodiment 2
[0031]In the sulfuric acid system, the Cr content in the mixed solution of chromium and iron is 20.0 g / L, and the content of Fe is 15.0 g / L. The reducing agent is sodium sulfite, and the sodium sulfite solution with a concentration of 20% and the mixed solution of chromium and iron are added dropwise at a 1:5 ratio. , add an appropriate amount of NaOH solution to adjust the pH of the solution to 2.0, add sodium phosphate according to the molar ratio of phosphate and chromium ions of 0.3, keep it at 70 °C for 90 min, control the stirring line speed at 300 m / min during the process, and filter to obtain phosphoric acid Chromium chromium hydroxide composite precipitate, the concentration of chromium and iron in the filtrate were 0.089 g / L and 14.89 g / L respectively, the recovery rate of chromium was 99.56%, the recovery rate of iron was 99.08%, and the separation coefficient of ferrochrome was 223.1.
Embodiment 3
[0033] In the sulfuric acid system, the Cr content in the chromium-iron mixed solution is 6.0 g / L, the Fe content is 3.0 g / L, the reducing agent is sodium thiosulfate, and the concentration of 10% sodium thiosulfate solution and chromium-iron mixed solution is 1 Add an appropriate amount of NaOH solution to adjust the pH of the solution to 1.5, add sodium phosphate according to the molar ratio of phosphate and chromium ions of 0.5, and keep warm at 80 °C for 60 min. During the process, the linear speed of stirring is controlled at 150 m / min, the composite precipitate of chromium phosphate and chromium hydroxide was obtained by filtration, the concentrations of chromium and iron in the filtrate were 0.053 g / L and 2.90 g / L respectively, the recovery rate of chromium was 99.10%, and the recovery rate of iron was 99.03%. Coefficient 109.4.
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