Denitration system for flue gas denitrification by utilizing ozone and spray tower
A spray tower and ozone technology, applied in the field of denitrification system, can solve the problems of easy decomposition of ozone and low oxidation effect
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Embodiment 1
[0072] combined with figure 1 , attached Figure 5 , the present invention is described:
[0073] The spray tower is a cylinder with a diameter of 0.8m, a tower height of 5m, and a wall thickness of 8mm, made of 304L stainless steel. A sprinkler 1 is installed at a position 1 meter away from the top of the tower, and the sprinkler 1 is composed of three 90° conical solid nozzles 2, which are evenly arranged in a cross section. The sprayer 1 is connected to the liquid inlet pipe 4 of the soluble lye; the ozone distributor 5 is located 0.8m below the sprayer 1, and the ozone distributor 5 is a flat spiral tube, and the lower part of the tube is evenly facing the direction of the flue gas There are several small holes of 1mm. The ozone distributor 5 is connected to the inlet pipe 6 of ozone. At a position 1.5m away from the bottom, the spray tower is provided with a flue gas inlet 7, and a flue gas outlet 8 is set at the top. The bottom of spray tower is used as lye tank 9. ...
Embodiment 2
[0079] combined with figure 2 , attached Figure 5 , the present invention is described:
[0080] The structure difference between this embodiment and the denitrification system described in Embodiment 1 is that: the ozone distributor 5 is located at a position of 2 meters below the shower 1; and the small hole of the ozone distributor 5 faces upward; the ozone passes through the ozone distributor The small hole of 5 ejects upwards, consistent with the flue gas flow. Other content and process are the same as embodiment 1.
[0081] Measured at the flue gas outlet 8 of the spray tower, the NO content is 43, 47, 48, 49 mg / m 3 Equal values, ranging from 40-50mg / m 3 between.
Embodiment 3
[0083] combined with image 3 , attached Figure 5 , the present invention is described:
[0084]The structure difference between this embodiment and the denitrification system described in Embodiment 1 is that: a shower 1-b is set at a position 0.5 meters above the shower 1; the shower 1-b is connected to the liquid inlet pipe 4-b, connect booster pump 12-b, flow regulating valve 13-b, and finally connect to lye tank 9. That is, the system has two sets of soluble lye supply systems. Other content and process are the same as embodiment 1.
[0085] Measured at the flue gas outlet 8 of the spray tower, the NO content is 57, 54, 44, 48 mg / m 3 Equivalent values, ranging from 45-60mg / m 3 between.
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