Treatment method of waste acid in titanium dioxide production process
A technology of production process and treatment method, which is applied in the direction of iron oxide, sulfate/bisulfate preparation, iron oxide/hydroxide, etc., which can solve the problem of high processing cost, large energy consumption, latent heat of phase change evaporation major issues
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Embodiment 1
[0007] In the 40 tons of 5% waste sulfuric acid produced in the rinsing process, 1.1 tons of quicklime was added, and the molar ratio of calcium oxide to sulfuric acid was 1:1. The generated calcium sulfate is precipitated and separated, and then 3.1 tons of sodium hydroxide with a mass concentration of 10% is added to the remaining solution, and the pH is about 8 at this time. The resulting precipitate was filtered, washed with tap water, and dried at 120° C. for 40 minutes to obtain 0.6 tons of magnetic ferric oxide particles.
Embodiment 2
[0009] In the 30 tons of 1% waste sulfuric acid produced in the rinsing process, 0.14 tons of quicklime was added, and the molar ratio of calcium oxide to sulfuric acid was 0.8:1. The generated calcium sulfate is precipitated and separated, and then 1.05 tons of potassium hydroxide with a mass concentration of 25% is added to the remaining solution, and the pH is about 7 at this time. The resulting precipitate was filtered, washed with tap water, and dried at 95° C. for 120 minutes to obtain 0.36 tons of magnetic iron ferric oxide particles.
Embodiment 3
[0011] In the 35 tons of 3% waste sulfuric acid produced in the rinsing process, 0.54 tons of quicklime was added, and the molar ratio of calcium oxide to sulfuric acid was 0.9:1. The generated calcium sulfate is precipitated and separated, and then 2.0 tons of sodium hydroxide with a mass concentration of 20% is added to the remaining solution, and the pH is about 7.5 at this time. The resulting precipitate was filtered, washed with tap water, and dried at 105° C. for 90 minutes to obtain 0.77 tons of magnetic ferric oxide particles.
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