Method of iron extraction and removal with solvent extraction agent
A technology for extracting iron and extracting agent, applied in the field of hydrometallurgy, can solve the problems of inappropriate use, long operation time, difficult iron stripping, etc., and achieve the effects of avoiding acid mist, reducing acidity, and improving stripping capacity.
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Embodiment 1
[0022] Iron-containing acidic wastewater produced by an enterprise contains 34.5g / L Fe 3+ and 24.3g / L H 2 SO 4 , use P204-kerosene system as organic phase extraction to remove iron, the volume percent concentration of P204 in the organic phase is 35%, and the loaded organic phase contains Fe16.2g / L. The loaded organic phase uses saturated sodium chloride solution of 2mol / L HCl hydrochloric acid as anti-iron agent, contacts according to O / A=0.3, contact time at 25°C for 10 minutes, three-stage countercurrent stripping, and the stripping rate of iron is 97.8% . The blank organic phase obtained by back-extraction was compared to O / A=1, then added a sulfuric acid solution with a pH of 0.5, stirred and washed for 10 minutes, and then returned to the iron extraction process for recycling. NaOH is added to the iron-containing aqueous phase obtained by stripping to adjust the pH of the solution to 6.5, and the filter residue and filtrate are obtained by filtration. The iron in the...
Embodiment 2
[0024] The solution with pH 0.8 obtained from stone coal oxidative roasting-acid leaching contains Fe 3+ 11.6gL, V 2 o 5 10.2gL, use P204-TBP-kerosene system as organic phase extraction to remove iron, the volume percentage concentration of P204 in the organic phase is 50%, and the loaded organic phase contains Fe5.3gL, V 2 o 5 0.7g / L. 1mol / L H 2 SO 4 The iron-rich organic phase obtained after back-extracting vanadium with a sulfuric acid solution, with 2mol / L BaCl 2Use the hydrochloric acid-chloride solution of 2mol / L NaCl and 0.2mol / L HCl as the antiferric agent, and contact the loaded organic phase with the antiferric agent according to O / A=3, stir at 15°C for 50min, separate the phases, and The stripping rate is 91.7%. Barium carbonate was added to the aqueous phase obtained by stripping, stirred at 30° C. for 1 h, the pH of the solution was adjusted to 2.5, and the iron-containing filter residue and chloride filtrate were obtained by filtration. The chloride filtr...
Embodiment 3
[0026] The sulfuric acid solution obtained by removing copper and impurity from the copper electrolyte contains Fe 3+ 8.5gL, H 2 SO 4 404.5g / L, use the P204-TBP-kerosene system as the organic phase to extract and remove iron, the volume percentage concentration of P204 in the organic phase is 25%, and the loaded organic phase contains Fe7.6gL. With 6mol / L CaCl 2 Use hydrochloric acid-calcium chloride solution of 1mol / L HCl as anti-iron agent, and the loaded organic phase is contacted with anti-iron agent according to O / A=2.5, stirred at room temperature for 45min, phase separation, and the stripping rate of iron is 92.3%. Add lime and Ca(OH)2 to the aqueous phase obtained by stripping, stir at 50°C for 0.5h, adjust the pH of the solution to 5.2, and filter to obtain iron-containing filter residue and calcium chloride filtrate. Calcium chloride filtrate is acidified by adding hydrochloric acid to obtain H+ concentration of 1mol / L hydrochloric acid-chloride solution, return t...
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