Deep dealkalizing method of red mud in alumina factory
A deep dealkalization and aluminum plant technology, applied in chemical instruments and methods, sludge treatment, water/sludge/sewage treatment, etc., can solve the problems of low concentration of waste liquid, high dealkalization efficiency, high cost of alkali recovery, etc. Achieve the effects of low process energy consumption, high dealkalization efficiency, and low process energy consumption
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Embodiment 1
[0019] Taking the red mud of an alumina plant in Henan as an example, the mass percentage (%) of the chemical composition of the red mud in the plant is as follows:
[0020]
[0021] Mix the red mud with the evaporated mother liquor with an alkali concentration of 200g / L, add quicklime so that the total calcium-silicon ratio of the slurry is 3, raise the temperature to 300°C, and react for 1.5 hours, and the liquid-solid ratio is 6. The slurry was naturally cooled to 110°C, then separated by filtration and washed. After the filter residue was dried and analyzed, the mass percent content of sodium oxide was 0.31%.
Embodiment 2
[0023] Mix the red mud of the alumina plant in Example 1 with the evaporated seed liquor with an alkali concentration of 300g / L, add quicklime according to the slurry Ca / Si ratio of 3, raise the temperature to 200°C, and react for 1.5 hours, with a liquid-solid ratio of 10. After the reaction, the slurry was naturally cooled to 110° C., filtered, washed, and the filter cake was dried. After analysis, the percentage content of sodium oxide in the final slag was 1.51%.
Embodiment 3
[0025] Mix the red mud of the alumina plant in Example 1 with the mother liquor with an alkali concentration of 260g / L, add quicklime according to the slurry Ca / Si ratio of 2, raise the temperature to 300°C, and react for 0.5 hours, with a liquid-solid ratio of 3. After the reaction, the slurry is pumped into the flash tank, flashed to 115°C, and then pumped into the filter for filtration. The obtained slag phase was fully washed and filtered. After the filter residue was dried, its sodium oxide percentage was analyzed to be 0.89%.
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