Method of dealkalizing red mud and recovering aluminum and iron
A technology for recycling aluminum and red mud, which is applied in chemical industry and construction materials, metallurgy and preparation of construction materials, and metallurgy, which can solve the problems of high processing cost and difficulty in industrialization, and achieve easy industrialization, low processing cost and process flow simple effect
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Embodiment 1
[0019] The liquid-solid ratio of a mixed solution of Bayer red mud and sulfuric acid is 3; the concentration of sulfuric acid is 30g / l; then the mixed solution is put into a heated and stirred container for stirring, the temperature is 110°C, and the stirring speed is 200r / l min, the leaching time is 20min, and then the solution is washed and filtered, the number of washings is 3 times, and the obtained filter residue is the treated red mud; the Na in the treated red mud 2 The O content is 0.85%. After neutralization precipitation and resin adsorption treatment, the recovery rates of aluminum and iron entering the solution are 82% and 90% respectively, and the purity of sodium sulfate after crystallization is greater than 92%.
Embodiment 2
[0021] The liquid-solid ratio of a mixed solution of Bayer red mud and sulfuric acid is 5; the concentration of sulfuric acid is 150 g / l; min, the leaching time is 70min, and then the solution is washed and filtered, the number of washings is 8 times, and the obtained filter residue is the treated red mud; the Na in the treated red mud 2 The O content is 0.21%. After neutralization precipitation and resin adsorption treatment, the recovery rates of aluminum and iron entering the solution are 75% and 88% respectively, and the purity of sodium sulfate after crystallization is greater than 93%.
Embodiment 3
[0023] The liquid-solid ratio of the mixed solution of red mud and sulfuric acid is 6; the concentration of sulfuric acid is 50g / l; then the mixed solution is put into a heated and stirred container for stirring, the temperature is 60°C, and the stirring speed is 500r / min, the leaching time is 70min, and then the solution is washed and filtered, the number of washings is 5 times, and the obtained filter residue is the treated red mud; the Na in the treated red mud 2 The O content is 0.41%. After neutralization precipitation and resin adsorption treatment, the recovery rates of aluminum and iron entering the solution are 70% and 94% respectively, and the purity of sodium sulfate after crystallization is greater than 85%. .
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