Method for producing high-efficiency purifying agent magnesium ferrous sulfate from titanium dioxide waste acid by using sulphuric acid method
A technology of magnesium ferrous sulfate and titanium dioxide waste acid, applied in magnesium sulfate, ferric sulfate, flocculation/sedimentation water/sewage treatment, etc., can solve the problem of ineffective treatment of severe sewage, complex equipment and processes, and increase production costs, etc. problem, to achieve the effect of simple and practical equipment, low production cost, simple and convenient operation and use
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Embodiment 1
[0023] Embodiment 1 The diameter of the reaction tank is 3 meters, and the height is 3 meters. In the reaction tank, 4.8 m of mother liquor water is put into (tap water is used when there is no mother liquor water), and the stirring speed of the agitator is 40 to 80 rpm. The Baume hydrometer measures the specific gravity of the mixed solution. When adding about 1 ton of magnesite containing 85% MgO, the specific gravity of the mixed solution is about 1.30 to 1.38 (the density of the Baume hydrometer). The method of specific gravity is used to control the addition of magnesite, and then gradually add waste sulfuric acid (containing 17-22% of sulfuric acid) produced in the production process of sulfuric acid titanium dioxide to the reaction tank until the pH value of the mixed solution is 3.5-4.0 Stop adding waste sulfuric acid, continue to stir, and control the reaction temperature at no more than 95°C to avoid boiling the mixed solution. After 1.5 hours of reaction, the pH valu...
example 2
[0026] Example 2 The reaction pool has a diameter of 3 meters and a height of 3 meters. Put 5m of mother liquid water into the reaction tank 3 , the stirring speed is 50-70 rpm. Gradually add magnesite with an MgO content of 90%. When the specific gravity of the mixed solution is 1.34 to 1.38 (Baume pycnometer density), the amount of magnesite will reach about 1 ton. At this time, the addition of magnesite can be stopped. , and then intermittently add waste sulfuric acid containing about 20% sulfuric acid to the reaction tank, control the reaction temperature at no more than 95°C, and stop adding waste sulfuric acid when the pH value of the mixed solution is 3.5 to 3.8. After 2.5 hours of reaction, the pH value of the mixed solution rose to 4.7-5.2, at this time the specific gravity of the mixed solution was about 1.40-1.45 (Baume hydrometer density), and the temperature was about 90°C. After the reaction, the mixed liquid is filtered with a plate and frame filter press, and...
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