Method for eliminating dioxins in flue gas
A technology for dioxin and flue gas, applied in separation methods, chemical instruments and methods, and separation of dispersed particles, etc., can solve the problems that the background technology cannot achieve and will offset the degradation effect, so as to achieve no equipment bottleneck and dioxin content The effect of reducing and the process is simple and easy
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Embodiment 1
[0019] A rotary kiln-type incinerator burns paper-making residues containing a large amount of plastics. The incineration capacity is 120 tons / day. The flue gas contains high concentrations of NOx, HCl, and SO. 2 After the heat recovery heating surface, the spray tower is used to spray lime and other lye to absorb the acid gas. The temperature of the flue gas entering the tower body is 360-380℃, and the temperature of the flue gas leaving the tower body is 180℃-200℃ , When the present invention is not adopted, the dioxin toxicity equivalent in the flue gas is 1.12ngI-TEQ / Nm 3 . During the implementation of the present invention, carbohydrazide is added to the alkaline spray liquid preparation tank used in the spray tower with a concentration of 0.10%wt. After use, the flue gas enters the bag filter at about 180°C, and the smoke after the dust collector The toxic equivalent of dioxin in the air is reduced to 0.1ngI-TEQ / Nm 3 .
Embodiment 2
[0021] A 350t / d grate type garbage incinerator adopts fly ash collected by electrostatic precipitator, and then uses wet spray tower system to purify acid gas, Hg, etc. in the flue gas. When the method of the invention is not used, the dioxin in the flue gas is exhausted. The toxic equivalent of dioxin is 0.225ngI-TEQ / g, and the toxic equivalent of dioxin in fly ash is 4.2ng I-TEQ / g. When the method of the present invention is implemented, a 1% wt carbohydrazide solution is sprayed into the flue temperature zone around 650℃ in front of the superheater, and the moisture content is evaporated in the range of 650℃~550℃, then enters the superheater, and finally exhausts the dioxins in the flue gas The toxicity equivalent is 0.05ngI-TEQ / Nm 3 , The toxicity equivalent of dioxin in fly ash is 0.8ng I-TEQ / g.
Embodiment 3
[0023] A fluidized bed waste incinerator is equipped with a heating surface after cyclone separation, and a semi-dry flue gas purification system is installed behind the heating surface. When the method of the present invention is not used, the dioxin toxicity equivalent in fly ash is 2.06ng I-TEQ / g, and the dioxin toxicity equivalent in flue gas is 0.6ng I-TEQ / Nm 3 . When the method of the present invention is implemented, the urea solution containing 4.6%wt hydrazine hydrate is sprayed into the inlet of the cyclone separator at a temperature of about 800°C to fully mix with the flue gas, and the automatic control system is used to control the spraying amount, so that the The smoke temperature drop caused by the process does not exceed 50-70℃. The toxic equivalent of dioxins in the final smoke is 0.078ngI-TEQ / Nm 3 , The dioxin toxicity equivalent in semi-dry fly ash is 0.42ngI-TEQ / g, and the NOx in exhaust smoke is reduced to below 43ppm.
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