A method for iron strengthening red mud dealkalization and separating and recovering iron
A technology for separation and recovery of red mud, which is applied in the field of comprehensive utilization of resources to achieve high desulfurization efficiency, low energy consumption, and improved dealkalization capacity.
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Embodiment 1
[0046] Grind and pulverize the red mud, the grinding particle size is 150 mesh, and then put it in the red mud pre-soaking tank and add water to make slurry. The liquid-solid ratio of red mud and water in the red mud pre-soaking tank is 2:1. The temperature in the medium is 40°C; then pass through the sulfur dioxide containing the initial concentration of 3000mg / m 3 At the same time, the red mud slurry in the red mud prepreg tank is aerated and oxidized, in which the aerated oxygen and the introduced SO 2 The volume ratio is 1: 3, and the 2 The flow rate of the flue gas is: 40mL / min; after the pre-soaking of the red mud mixture is completed, filter to obtain the leaching solution and the red mud leaching residue after dealkalization, take the leaching solution and adjust its pH to 12, at this time Fe(OH) 3 Precipitation filtration; Fe(OH) obtained by filtration 3 Precipitation, 1 / 3 Fe(OH) 3 The precipitate is washed 5 times with distilled water and returned to the red mud ...
Embodiment 2
[0048] Grind and pulverize the red mud, the grinding particle size is 200 mesh, and then put it in the red mud presoak tank and add water to make slurry. The liquid-solid ratio of red mud and water in the red mud presoak tank is 3:1, and control the The temperature in the medium is 50°C; then pass through the sulfur dioxide containing the initial concentration of 3000mg / m 3 At the same time, the red mud slurry in the red mud prepreg tank is aerated and oxidized, in which the aerated oxygen and the introduced SO 2 The volume ratio is 1: 5, and the SO 2 The flow rate is: 40mL / min; after the red mud mixture is pre-soaked, filter to obtain the leaching solution and red mud leaching residue after dealkalization, take the leaching solution and adjust its pH to 13, at this time Fe(OH) 3 Precipitation filtration; Fe(OH) obtained by filtration 3 Precipitation, 1 / 3 Fe(OH) 3 The precipitate is washed 7 times with distilled water and returned to the red mud presoak tank in step (1) fo...
Embodiment 3
[0050] Grind and pulverize the red mud, the grinding particle size is 230 mesh, and then put it in the red mud pre-soaking tank and add water to slurry. The liquid-solid ratio of red mud and water in the red mud pre-soaking tank is 4:1. The temperature in the medium is 60°C; then pass through the sulfur dioxide containing the initial concentration of 2500mg / m 3 At the same time, the red mud slurry in the red mud prepreg tank is aerated and oxidized, in which the aerated oxygen and the introduced SO 2 The volume ratio is 1: 7, and the SO 2 The flow rate is: 40mL / min; after the red mud mixture is pre-soaked, filter to obtain the leaching solution and red mud leaching residue after dealkalization, take the leaching solution and adjust its pH to 13, at this time Fe(OH) 3 Precipitation filtration; Fe(OH) obtained by filtration 3 Precipitation, 1 / 3 Fe(OH) 3 The precipitate is washed with distilled water for 9 times and returned to the red mud presoak tank in step (1) for red mud...
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