Method for eliminating water mist from wet desulfurization flue gas
A wet desulfurization and flue gas technology, applied in coal-fired power plants, environmental protection, and smelting fields, can solve the problems of lower net flue gas discharge temperature, fine liquid droplet entrained emission, and impact on residents' lives, so as to achieve low operating power consumption and increase environmental protection benefit, the effect of increasing desulfurization efficiency
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Embodiment 1
[0025] This embodiment is the implementation of the elimination method of wet flue gas water mist, such as figure 1 As shown, the treatment object is the desulfurized flue gas water mist using the limestone-gypsum wet desulfurization process (WFGD). Primary flue gas 1 without desulfurization treatment (sulfur content is about 450mg / Nm 3 ) enters from the flue gas inlet at the bottom of the desulfurization tower 2, and after wet desulfurization, the hot flue gas 3 (with a sulfur content of about 25 mg / Nm) is discharged from the upper flue gas outlet of the desulfurization tower 2 3 ,) into the heat exchanger 4, and exchange heat with the air 5 that enters countercurrently on the heat exchange surface of the heat exchanger 4. The heat exchange surface of the heat exchanger used for heat exchange is made of metal surface coated with acid corrosion resistant coating material, or organic polymer material, or metal titanium, which has good corrosion resistance. The cooled flue gas...
Embodiment 2
[0028] This embodiment is the implementation of the elimination method of wet flue gas water mist, such as figure 2 As shown, the treatment object is the desulfurized flue gas water mist using the limestone-gypsum wet desulfurization process (WFGD). The processing flow of this embodiment is substantially the same as that of Embodiment 1, the difference is that the primary flue gas 1 that has not been desulfurized is exchanged with the heated air 8 discharged from the heat exchanger 4 in the heat exchanger 12. heat, make the untreated first flue gas 1 heat exchange and heat up and then enter the desulfurization tower 2 to repeat the operation process in Example 1. The hot air 13 heated up again through heat exchange enters the flue gas dehydrator 7, and this embodiment 2 can realize the secondary utilization of the air.
[0029] Through the indirect heat exchange between flue gas and air after wet desulfurization through heat exchanger, the flue gas is cooled and cooled, and ...
Embodiment 3
[0031] This embodiment is the implementation of the elimination method of wet flue gas water mist, such as image 3 As shown, the treatment object is the desulfurized flue gas water mist using the limestone-gypsum wet desulfurization process (WFGD). The treatment process of this embodiment is substantially the same as that of Example 1, except that the hot flue gas 3 after desulfurization treatment is first processed by lye 14 to neutralize the residual desulfurization liquid before entering the heat exchanger 4 and exchanging heat with air 5 The dilute sulfuric acid then enters the heat exchanger 4 for heat exchange, and the treated lye 15 is discharged from the bottom of the heat exchanger 4 .
[0032] Desulfurized hot flue gas (sulfur content about 25mg / Nm 3 ), and then enter the heat exchanger for heat exchange after being treated with lye. The advantage of this embodiment is that the hot flue gas is firstly treated with lye, which can neutralize the residual dilute sulfu...
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