Method for mineralizing precipitated iron from zinc hydrometallurgy lixivium
A technology of hydrometallurgy and leaching solution, which is applied in the field of chemical industry and metallurgy, can solve the problems of high disposal cost, low separation efficiency of zinc and iron, and high content of heavy metals, and achieve low content of harmful elements, high separation efficiency of zinc and iron, mineralization and precipitation of iron high rate effect
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Embodiment 1
[0030] A method for mineralizing and precipitating iron from a zinc hydrometallurgical leaching solution, the specific steps of which are as follows: take 5.0 L of the leaching solution containing zinc sulfate and ferrous sulfate produced by a wet zinc smelting production enterprise, and add it to a reaction kettle. The zinc ion concentration in the leaching solution is 130 g / L, and the iron ion concentration is 15 g / L. After heating the solution to 100°C, industrial oxygen with an oxygen content of 88% was introduced, and the oxygen partial pressure was controlled to be 0.3MPa, and then high-temperature steam was further introduced to maintain the reaction temperature at 135°C. 20 minutes after the oxygen was introduced into the reaction, the slurry of zinc oxide with a slurry concentration of 30% was pumped, and the zinc content in the zinc oxide was 62%. The pH value of the end point of the reaction was controlled to be 1.0, and the total reaction time was 180 minutes. Afte...
Embodiment 2
[0032] A method for mineralizing and precipitating iron from a zinc hydrometallurgical leaching solution, the specific steps of which are as follows: take 5.0 L of the leaching solution containing zinc sulfate and ferrous sulfate produced by a wet zinc smelting production enterprise, and add it to a reaction kettle. The zinc ion concentration in the leaching solution is 145g / L, and the iron ion concentration is 6.5g / L. After heating the solution to 90°C, industrial oxygen with an oxygen content of 80% was introduced, and the oxygen partial pressure was controlled to be 0.1 MPa, and then high-temperature steam was further introduced to maintain the reaction temperature at 100°C. 30 minutes after the reaction started by feeding oxygen, the slurry of zinc oxide with a slurry concentration of 30% was pumped, and the content of zinc in the zinc oxide was 60%. The pH value of the end point of the reaction was controlled to be 2.0, and the total reaction time was 90 minutes. After th...
Embodiment 3
[0034] A method for mineralizing and precipitating iron from a zinc hydrometallurgical leaching solution, the specific steps of which are as follows: taking 5.0 L of the leaching solution containing zinc sulfate and ferrous sulfate produced by a hydrometallurgical zinc smelting enterprise, and adding it to a reaction kettle. The zinc ion concentration in the leaching solution is 120.0g / L, and the iron ion concentration is 25.5g / L. After heating the solution to 100°C, industrial oxygen with an oxygen content of 90% was introduced, and the partial pressure of oxygen was controlled to be 0.5MPa, and then high-temperature steam was further introduced to maintain the reaction temperature at 135°C. Twenty-five minutes after the start of the reaction by introducing oxygen, the slurry of zinc oxide with a slurry concentration of 45% was pumped, and the content of zinc in the zinc oxide was 65%. The pH value of the end point of the reaction was controlled to be 0.8, and the total react...
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