Flue gas desulfurization and denitration system and method
A technology for desulfurization, denitrification and desulfurization systems, applied in the field of flue gas desulfurization and denitrification systems, can solve problems such as difficulty in popularization, poor desulfurization and denitrification effects, etc., and achieve the effects of wide application range, good adjustment characteristics, and guaranteed stability
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[0068] Example 1
[0069] Such as figure 1 As shown, a flue gas desulfurization and denitrification system includes a pre-dust collector 1, a rotary spray desulfurization and denitrification system 3, an induced draft fan 6 and a chimney 10 arranged in sequence, the pre-dust collector 1, a rotary spray desulfurization and denitrification system 3, and an induced draft fan 6 and the chimney 10 are connected in sequence through a flue, and the rotary spray desulfurization and denitration system 3 is used for preliminary desulfurization and denitration of the flue gas, wherein SO 2 Partially removed, NOx is oxidized to high-valence NO 2 And N 2 O 5 A circulating fluidized bed desulfurization system 5 is provided between the rotary spray desulfurization and denitrification system 3 and the induced draft fan 6, and is connected in sequence through a flue. Most of the unreacted slaked lime in the rotary spray desulfurization and denitrification system 3 The powder enters the circulating...
Example Embodiment
[0077] Example 2
[0078] The basic structure of a flue gas desulfurization and denitrification system of this embodiment is the same as that of embodiment 1. The difference and improvement are that:
[0079] Such as image 3 As shown, the rotary spray desulfurization and denitrification system 3 includes a rotary spray desulfurization and denitration reaction tower 31 and a self-flowing high-level emulsion tank 32. The self-flowing high-level emulsion box 32 is arranged above the top of the rotary spray desulfurization and denitration reaction tower 31. The forced oxidized slaked lime milk in the self-flowing high-position emulsion tank 32 flows into the high-speed centrifugal atomizer in the rotating spray desulfurization and denitrification reaction tower 31 through the gravity pipe set at the bottom of the self-flowing high-position emulsion tank 32 by gravity, Participate in the oxidation reaction in the rotating spray desulfurization and denitration reaction tower 31 after at...
Example Embodiment
[0084] Example 3
[0085] Such as image 3 As shown, the basic structure of a flue gas desulfurization and denitrification system of this embodiment is the same as that of Embodiment 2. The difference and improvement lies in that, further, the rotating spray desulfurization and denitration reaction tower 31 is provided with two-sided shafts at the bottom of the tower. To exhaust device 33, the axial exhaust device 33 on both sides is a T-shaped structure in which two steel pipes are connected and fixed at 90° to each other. The two steel pipes are vertical along the axis of the rotating spray desulfurization and denitration reaction tower 31. Straight installation, the other horizontal installation, the flue gas enters from the two ends of the vertical steel pipe, and then is discharged from the horizontal steel pipe; the flue gas is axially discharged from the upper and lower air inlets of the axial exhaust device 33 on both sides , It will not affect the rotating airflow in the...
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