Application method of fine desulfurization in sulfuric acid exhaust absorption
An application method, fine desulfurization technology, applied in separation methods, chemical instruments and methods, separation of dispersed particles, etc.
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Embodiment 1
[0031] A. Introduce the sulfur-containing tail gas into the recovery tower;
[0032] B. Spray the ammonium sulfite-ammonium bisulfite solution with a pH value of 5.6 from the top of the tower to absorb SO in the sulfur-containing tail gas 2 and SO 3 , adjust the circulating volume of fine desulfurization solution ammonium sulfite-ammonium bisulfite solution through the pump, adjust the gas-liquid ratio to 370:1, reduce the resistance, enhance the absorption effect, the absorption rate reaches 87%, and the tail gas after absorption reaches the national emission standard , discharged into the atmosphere through the vent chimney; the temperature of the absorption mother liquor is between 25-30°C, and it flows back from the bottom of the absorption tower to the mother liquor circulation tank, in order to ensure that the ammonium sulfite-ammonium bisulfite solution (NH 4 ) 2 SO 3 with NH 4 HSO 3 The ratio remains constant, adding mass concentration is 10.3% dilute ammonia to a...
Embodiment 2
[0036] A. Introduce the sulfur-containing tail gas into the recovery tower;
[0037] B. Spray the ammonium sulfite-ammonium bisulfite solution with a pH value of 6.1 from the top of the tower to absorb SO in the sulfur-containing tail gas 2 and SO 3 , adjust the circulating volume of fine desulfurization solution ammonium sulfite-ammonium bisulfite solution through the pump, adjust the gas-liquid ratio to 350:1, reduce the resistance, enhance the absorption effect, the absorption rate reaches 82%, and the tail gas after absorption reaches the national emission standard , discharged into the atmosphere through the vent chimney; the temperature of the absorption mother liquor is between 25-30°C, and it flows back from the bottom of the absorption tower to the mother liquor circulation tank, in order to ensure that the ammonium sulfite-ammonium bisulfite solution (NH 4 ) 2 SO 3 with NH 4 HSO 3 The ratio remains constant, adding mass concentration is 10.46% dilute ammonia to ...
Embodiment 3
[0041] A. Introduce the sulfur-containing tail gas into the recovery tower;
[0042] B. Spray the ammonium sulfite-ammonium bisulfite solution with a pH value of 5.8 from the top of the tower to absorb SO in the sulfur-containing tail gas 2 and SO 3 , adjust the circulating volume of fine desulfurization solution ammonium sulfite-ammonium bisulfite solution through the pump, adjust the gas-liquid ratio to 360:1, reduce the resistance, enhance the absorption effect, the absorption rate reaches 93%, and the tail gas after absorption reaches the national emission standard , discharged into the atmosphere through the vent chimney; the temperature of the absorption mother liquor is between 25-30°C, and it flows back from the bottom of the absorption tower to the mother liquor circulation tank. 4 ) 2 SO 3 with NH 4 HSO 3 The ratio remains constant, adding mass concentration is 10.5% dilute ammonia to adjust.
[0043] C. Add sulfuric acid to decompose in step B: the excess moth...
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