Red mud dealkalization method
A red mud and dealkalization technology, which is applied in chemical instruments and methods, sludge treatment, water/sludge/sewage treatment, etc., can solve the problems of high dealkalization cost, cumbersome operation, and long dealkalization time, and achieve dealkalization The alkali time is shortened, the removal effect is good, and the operation is simple
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Embodiment 1
[0029] Embodiment one: a kind of method of dealkalization of red mud
[0030] The method comprises a dilute sulfuric acid dealkalization process and a calcium oxide dealkalization process under pressurized conditions, and its detailed steps are as follows:
[0031] a. Dilute sulfuric acid dealkalization: first analyze the alkali content in the red mud, prepare it into a slurry, the solid content of the slurry is 50%, import the prepared slurry into a fast grinder for grinding, and then grind it according to the alkali content The required concentration is 8% sulfuric acid slowly added in the slurry, the addition of the sulfuric acid is according to the chemical reaction 2K + +2Na + +2SO 4 2- =Na 2 SO 4 +K 2 SO 4 1.3 times the amount of sulfuric acid required, the particle size of the red mud after grinding for 45 minutes is less than 10 microns, filter and wash the ground red mud to obtain a filter cake, and analyze the alkali content in the obtained filter cake by conv...
Embodiment 2
[0033] Embodiment two: basically the same as embodiment one, the similarity is no longer described, and the difference is:
[0034] The concentration of dilute sulfuric acid in step a is 6%, and its add-on is according to chemical reaction 2K + +2Na + +2SO 4 2- =Na 2 SO 4 +K 2 SO 4 2 times of the required amount of sulfuric acid, the solid content of the prepared slurry is 45%, and the time for importing into the fast grinder for grinding is 50 minutes;
[0035] The amount of calcium oxide added in the step b is 4 times of the amount of calcium oxide required according to the chemical reaction KNaR+CaO=KNaO+CaR, the solid content of the slurry is 60%, and the reaction temperature in the autoclave is 120°C. The time is 20 minutes, and the obtained filter cake is dried with a drum dryer at a drying temperature of 150°C.
Embodiment 3
[0036] Embodiment three: basically the same as embodiment one, the similarity is no longer described, and the difference is:
[0037] The concentration of dilute sulfuric acid in step a is 9%, and its addition is according to chemical reaction 2K + +2Na + +2SO 4 2- =Na 2 SO 4 +K 2 SO 4 0.5 times of the required amount of sulfuric acid, the solid content of the prepared slurry is 30%, and the time for importing into the fast grinder for grinding is 30 minutes;
[0038] The amount of calcium oxide added in step b is 6 times the amount of calcium oxide required according to the chemical reaction KNaR+CaO=KNaO+CaR, the solid content of the slurry is 35%, and the reaction temperature in the autoclave is 150°C. The time is 5 minutes, and the obtained filter cake is dried under the condition of 180°C by airflow drying method.
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