Wet flue gas desulphurization dedusting tower and wet flue gas desulphurization dedusting method
A technology of wet desulfurization and dedusting tower, which is applied to chemical instruments and methods, separation methods, and separation of dispersed particles. It can solve problems such as difficulty in removal, difficulty in charging, and insufficient absorption of flue gas. Simple maintenance and high efficiency
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Embodiment 1
[0030] Such as figure 1 As shown, a flue gas wet desulfurization and dust removal tower includes a tower body, a spray layer 1, and a demister layer 2 above the spray layer. It is characterized in that a flue gas Special bubbling system for wet desulfurization and dust removal 3.
[0031] Such as Figure 4 , Figure 5 and Figure 6 As shown, the special bubbling system 3 for flue gas wet desulfurization and dust removal includes a number of flue gas pipes 31, bubbling pipes 32 on the side walls of the flue gas pipes 31, and a delivery subsystem 33 for absorbing wetting liquid. The bubbler tube 32 is provided with a liquid vapor bubble releasing device 321 in the form of a small hole, which is used to blow out the liquid bubbles into the flue gas tube 31. connect.
[0032] The flue gas pipe 31 in this embodiment is hexagonal, and a plurality of flue gas pipes 31 can form a seamless splicing, and the bubbling pipe 32 is just located at the splicing corner of the three flue ...
Embodiment 2
[0036] Such as figure 2 As shown, another flue gas wet desulfurization dedusting tower. The difference between the flue gas wet desulfurization and dedusting tower in this embodiment and embodiment 1 is that on the basis of embodiment 1, a layer of mist eliminator is set above the special bubbling system 3 for flue gas wet desulfurization and dust removal Layer 2. The function of this demister layer 2 is to intercept the mist entrained in the flue gas after passing through the special bubbling system 3 for flue gas wet desulfurization and dust removal, so as to further remove the residual SO in the flue gas 2 and ultrafine particulate matter.
[0037] Such as Figure 7 As shown, the flue gas pipe 31 in this embodiment is quadrangular, and a plurality of flue gas pipes 31 form a seamless splicing, and the bubbling pipe 32 is located at the center of the side wall of each flue gas pipe 31 . The size and number of flue gas pipes 31 are configured according to the size of the...
Embodiment 3
[0039] like water image 3 As shown, another flue gas wet desulfurization dedusting tower. The difference between the flue gas wet desulfurization and dedusting tower in this embodiment and embodiment 1 is that on the basis of embodiment 1, a horizontal flue 4 is set above the special bubbling system 3 for flue gas wet desulfurization and dust removal, and the The flue gas is led out of the desulfurization and dust removal tower, and then a special demister 5 for the flue is installed on the horizontal flue. The special demister for the flue is a more mature product.
[0040] Like embodiment 2, under the situation that a conventional mist eliminator layer 2 is arranged directly above the special bubbling system 3 for wet desulfurization and dust removal of flue gas, the mist droplets intercepted by the mist eliminator 2 gather into falling water droplets, and the water droplets fall When reaching the flue gas pipe 31 of the special bubbling system 3 for wet flue gas desulfur...
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