Jacking flue gas processing device and method
A flue gas treatment, top entry technology, applied in separation methods, chemical instruments and methods, dispersed particle separation, etc., to achieve superior ammonia escape control effect, control of ammonia escape loss, and compact equipment.
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Embodiment 1
[0046] A 260T / h coal-fired power boiler uses high-sulfur coal with a sulfur content of 3.0%, and its flue gas flow rate is 320,000m 3 / h, flue gas containing sulfur dioxide 8,500mg / Nm 3 , containing smoke dust 80mg / Nm 3 , the content of other components, such as sulfur trioxide, nitrogen oxide and hydrogen chloride or hydrogen fluoride, could not be determined, and the flue gas temperature was 135°C.
[0047] With the desulfurization method of the present invention, flue gas containing pollutants such as sulfur dioxide and soot and having a temperature greater than 100°C, or called raw flue gas, enters the absorber 10 from the flue gas inlet 104 at the top of the desulfurization tower 1, and is absorbed After the flue gas distributor 11 installed in the device 10 is evenly distributed, it contacts with the absorption liquid mist droplets containing ammonia sprayed upward from the absorption liquid sprayer 12 at the same time in countercurrent and downstream contact, mixing, h...
Embodiment 2
[0054] A 260T / h coal-fired power boiler uses high-sulfur coal with a sulfur content of 0.6%, and its flue gas flow rate is 320,000m 3 / h, flue gas containing sulfur dioxide 1400mg / Nm 3 , containing smoke dust 40mg / Nm 3 , the content of other components, such as sulfur trioxide, nitrogen oxide and hydrogen chloride or hydrogen fluoride, could not be determined, and the flue gas temperature was 125°C.
[0055] Adopt the method of the present invention, be identical with embodiment 1.
[0056] The raw material ammonia is ammonia water with an ammonia content of 18.0%, and the addition amount is 1260kg / h, and the pH value of the absorption liquid is maintained at 5.3. The ammonia water is continuously added to the absorption liquid, and the addition position is on the absorption liquid circulation line 3, specifically The ammonia arranged on the circulation pipe 3 between the absorption liquid circulation outlet 109 of the oxidation crystallizer 20 and the inlet of the circulati...
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