Flue gas desulfurization and dust removal integrated device and process and application
A technology for desulfurization, dust removal, and flue gas, which is applied in the direction of gas treatment, combined devices, chemical instruments and methods, etc., can solve problems such as high SO2 content, low efficiency of waste gas treatment, and environmental protection pressure, so as to improve the surrounding environmental protection situation and increase environmental protection The effect of low efficiency and equipment operation cost
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Embodiment 1
[0042] Such as figure 1 As shown, the present invention divides the traditional desulfurization tower in a circular direction, so that each layer after division forms an independent circulation through its own circulation pump. The wet electrostatic demisting device is arranged on the top of the desulfurization tower to reduce the equipment footprint and increase space utilization. The ammonia water is injected into the ammonia addition tank through the special nozzle, and the ammonia water is directly pumped into the desulfurization tower absorption layer spray device through the absorption circulation pump to form NH 3 , (NH 4 ) 2 SO 3 In the high-concentration area, the high-concentration absorption liquid reacts with the high-sulfur flue gas in the absorption layer to generate part of NH 4 HSO 3 , NH 4 HSO 3 Return to the ammonia adding tank through the absorption layer return line, and react with high concentration ammonia water to be reduced to (NH 4 ) 2 SO 3 ,...
Embodiment 2
[0045] An integrated device for flue gas desulfurization and dust removal, comprising: a desulfurization tower, the desulfurization tower is sequentially provided with an oxidation tank 2, a concentration layer 4, an absorption layer 7, a recovery layer 9, a washing layer 11, and a mechanical defogging layer 13. Electrostatic demisting layer 14; the top of the desulfurization tower is provided with a flue gas outlet 15, the flue gas inlet 3 is located on the side wall of the desulfurization tower and below the concentrated layer 4, and the bottom of the desulfurization tower is also provided with an ammonia addition pool 1.
[0046] In some embodiments, the liquid outlet of the ammoniation tank 1 is connected to the liquid inlet of the absorption layer 7 .
[0047] In some embodiments, an absorption layer return pipe is arranged below the absorption layer 7 , and the absorption layer return pipe is connected to the ammonia addition tank 1 .
[0048] In some embodiments, the l...
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