Method using catalytic oxidation of sulfur dioxide tail gas for PH adjustment agent of phosphate rock ore dressing
A technology of sulfur dioxide and catalytic oxidation, applied in chemical instruments and methods, separation methods, dispersed particle separation, etc., can solve the problems of complex flotation effect and consumption, and achieve the effect of simple process, reduced side effects, and reduced effective content
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Embodiment 1
[0026] With phosphorus raw ore pulp (mass fraction of main chemical components in phosphorus raw ore powder: P 2 o 5 22.4%; MgO7.0%; SiO 2 : 18.4%; CaO: 30.7%; Fe 2 o 3 :1.6%; GeO 2 : 0.06%, CuO: 0.01%. -200 mesh content 92%, the solid content of the phosphate rock slurry formed with water is 47%), iron, germanium and copper are metal ions as catalysts, adding EDTA disodium buffer with a mass fraction of 0.08, in the dynamic wave desulfurization tower (The desulfurization temperature is controlled at 55°C; the sulfur dioxide tail gas flow rate is 26m / s; the liquid-gas volume ratio is 1 (m 3 )︰0.5 (L)) form a countercurrent contact with the sulfur dioxide tail gas from the absorption tower, and form a sulfuric acid solution after absorbing sulfur dioxide to decompose the raw phosphorus ore pulp. The tail gas after desulfurization treatment reaches 320mg / m3 of the new national standard tail gas 3 Emission Standards.
Embodiment 2
[0028] With phosphorus raw ore pulp (mass fraction of main chemical components in phosphorus raw ore powder: P 2 o 5 22.6%; MgO6.3%; SiO 2 : 16.9%; CaO: 33.2%; Fe 2 o 3 :2.0%; GeO 2 : 0.05%, CuO: 0.01%. The content of -200 mesh is 92%, the content of -200 mesh is 94%, and the solid content of the phosphate rock slurry formed with water is 51%. Metal ions such as iron, germanium and copper are used as catalysts, and EDTA disodium with a mass fraction of 0.06 and 0.05 Sodium citrate buffer, in the power wave desulfurization tower (the desulfurization temperature is controlled at 87°C; the sulfur dioxide tail gas flow rate is 23m / s; the liquid-gas volume ratio is 1 (m 3 ): 0.6 (L)) form a countercurrent contact with the sulfur dioxide tail gas from the absorption tower, absorb sulfur dioxide and form a sulfuric acid solution to decompose the raw phosphorus ore pulp. The tail gas after desulfurization treatment reaches 300mg / m3 of the new national standard tail gas 3 Emissi...
Embodiment 3
[0030] With phosphorus raw ore pulp (mass fraction of main chemical components in phosphorus raw ore powder: P 2 o 522.8%; MgO7.2%; SiO 2 : 19.9%; CaO: 31.5%; Fe 2 o 3 :2.2%; GeO 2 : 0.03%, CuO: 0.02%. -200 mesh content 90%, the solid content of the phosphate rock slurry formed with water is 53%), metal ions such as iron, germanium and copper are catalysts, adding a mass fraction of 0.15 sodium phosphate solution, in the power wave desulfurization tower (desulfurization temperature Control at 110°C; sulfur dioxide tail gas flow rate is 22m / s; liquid-gas volume ratio is 1 (m 3 ): 0.7 (L)) to form a countercurrent contact with the sulfur dioxide tail gas from the absorption tower, and form a sulfuric acid solution after absorbing sulfur dioxide to decompose the raw phosphorus ore pulp. The tail gas after desulfurization treatment reaches 315mg / m3 of the new national standard tail gas 3 Emission Standards.
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