Method for producing silicon dioxide hydrate from silicon recovered from wet-process phosphoric acid reaction flue gas
A technology of hydrated silica and wet-process phosphoric acid, which is applied in the direction of silica, silica, chemical instruments and methods, etc., to reduce labor intensity, prolong production cycle, and reduce blockage of equipment pipelines
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Embodiment 1
[0017] Example 1: First, 1.2 tons of solid ammonium fluoride is prepared into 10 tons of absorbent; it is prepared into an ammonium fluoride absorption solution with a mass fraction of 12% and a pH value of 6.0; then pump the absorption solution into the wet-process phosphoric acid tail washing device for Circularly absorb the fluorine-containing silicon gas in the wet-process phosphoric acid reaction flue gas, and control the absorption temperature at 55°C; when the mass percentage ratio of nitrogen and fluorine in the absorption liquid is controlled at 3.5, feed ammonia gas, and when the pH reaches 8.7, Hydrated silica was obtained after filtration.
Embodiment 2
[0018] Example 2: First, 2.5 tons of solid ammonium fluoride is prepared into 10 tons of absorbent; it is prepared into an ammonium fluoride absorption solution with a mass fraction of 26% and a pH value of 6.5; then pump the absorption solution into the wet-process phosphoric acid tail washing device for Circularly absorb the fluorine-containing silicon gas in the wet-process phosphoric acid reaction flue gas, and control the absorption temperature at 45°C; control the ratio of nitrogen and fluorine mass percentages in the absorption liquid to 4.0, and feed ammonia gas until the pH reaches 9.0. Hydrated silica was obtained after filtration.
Embodiment 3
[0019] Example 3: First, 2.5 tons of solid ammonium fluoride is prepared into 10 tons of absorbent; it is prepared into an ammonium fluoride absorption solution with a mass fraction of 26% and a pH value of 7.0; then pump the absorption solution into the wet phosphoric acid tail washing device for Circularly absorb the fluorine-containing silicon gas in the wet-process phosphoric acid reaction flue gas, and control the absorption temperature at 40°C; control the ratio of nitrogen and fluorine mass percentages in the absorption liquid to 3.5, feed ammonia gas, and carry out the process when the pH reaches 9.2. Hydrated silica was obtained after filtration.
[0020] Adopt the method of above-mentioned 3 embodiments, the fluorine yield in wet process phosphoric acid reaction flue gas reaches 99.52%, silicon yield reaches 99.50%; Recover the fluorine 2194 tons / year in wet process reaction flue gas, reclaim wet process reaction flue gas The silicon in the gas is 850 tons / year; th...
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