Device and method for eliminating colored smoke plume generated during wet desulphurization
A wet desulfurization and non-ferrous technology, applied in separation methods, chemical instruments and methods, and dispersed particle separation, etc., can solve the problems of reduced service life of heat exchangers, large volume of flue gas coolers outside the tower, and high dew point temperature. The effect of reducing the heat load of heating and eliminating colored plume and gypsum rain
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Embodiment 1
[0032] The boiler flue gas volume of a 300MW unit is 1.1 million Nm 3 / h, the temperature is 145°C, the concentration of sulfur dioxide is 2400mg / Nm 3 , the particle concentration is 30mg / Nm 3 . The desulfurization process adopts the limestone gypsum method, and the water washing cooling system and the flue gas heat exchange system of the present invention are added on the basis of the traditional and mature limestone gypsum method.
[0033] The flue gas first enters the flue gas cooler 15 on the inlet flue of the wet desulfurization absorption tower 1, and transfers heat to the heat medium water, so that the temperature of the heat medium water rises, and the flue gas temperature decreases to about 110°C and enters the wet desulfurization absorption tower 1. The above-mentioned flue gas passes through the desulfurization spray layer 3 upward in the wet desulfurization absorption tower 1, and is in countercurrent contact with the absorption liquid sprayed by the desulfurizat...
Embodiment 2
[0038] One 435m 2 Sintering machine with flue gas volume of 1.6 million Nm 3 / h, the temperature is 135°C, the concentration of sulfur dioxide is 1500mg / Nm 3 , the particle concentration is 50mg / Nm 3 . The desulfurization process adopts the limestone gypsum method, and the water washing cooling system and the flue gas heat exchange system of the present invention are added on the basis of the traditional and mature limestone gypsum method.
[0039] The flue gas first enters the flue gas cooler 15 on the inlet flue of the wet desulfurization absorption tower 1, and transfers heat to the heat medium water, so that the temperature of the heat medium water rises, and the flue gas temperature decreases to about 110°C and enters the wet desulfurization absorption tower 1. The above-mentioned flue gas passes through the desulfurization spray layer 3 upward in the wet desulfurization absorption tower 1, and is in countercurrent contact with the absorption liquid sprayed by the desu...
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