Process and system for reducing particle content after flue gas desulfurization
A particle and flue gas technology, which is applied in the process and system field of particle content in flue gas, can solve the problem of large content in the outlet of the desulfurization system, achieve the effects of reducing the content of fine particles, simple structure, and avoiding pollution
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Embodiment 1
[0030] Such as figure 1 , a limestone-gypsum desulfurization system, including a desulfurization tower 10, a first slurry pool 101 is arranged at the bottom of the desulfurization tower 10, a flue gas inlet 108 is provided at the lower part of the desulfurization tower 10, and a desulfurization stage 102 is located above the flue gas inlet 1087 in the desulfurization tower 10 , the desulfurization stage 102 is divided into at least two sections, the first section of the desulfurization stage 102 (the first desulfurization stage in contact with the flue gas) is connected to the first slurry pool 101 through the circulation pump 114 of the first section, and the last section of the desulfurization stage 102 passes through the first section The circulating pump 115 of the second section is connected to the second slurry tank 110; the first mist eliminator 103 is arranged above the desulfurization stage 102, and the first mist eliminator 103 is connected to the spray section 104, a...
Embodiment 2
[0036] Such as figure 2, a limestone-gypsum desulfurization system, including a desulfurization tower 20, a first slurry pool 201 is arranged at the bottom of the desulfurization tower 20, a flue gas inlet 208 is provided at the bottom of the desulfurization tower 20, and a desulfurization stage 202 is located above the flue gas inlet 208 in the desulfurization tower 20, The desulfurization stage 202 is divided into at least two sections. The first section of the desulfurization stage 202 (the front desulfurization stage that first contacts with the flue gas) is connected to the first slurry pool 201 through the circulation pump 214 of the first section, and the last section of the desulfurization stage 202 is passed through the second The circulating pump 215 of the section is connected to the second slurry tank 210; the first demister 203 is arranged above the desulfurization stage 202, and the first demister 203 is connected to the spray section 204, and the spray section 2...
Embodiment 3
[0041] Such as image 3 , a limestone-gypsum desulfurization system, including a desulfurization tower 30, a first slurry pool 301 is arranged at the bottom of the desulfurization tower 30, a flue gas inlet 307 is provided at the bottom of the desulfurization tower 30, and a desulfurization stage 302 is located above the flue gas inlet 307 in the desulfurization tower 30, The desulfurization stage 302 is divided into at least two sections. The first section of the desulfurization stage 302 (the front desulfurization stage that first contacts with the flue gas) is connected to the first slurry pool 301 through the circulation pump 314 of the first section, and the last section of the desulfurization stage 302 is passed through the second The circulating pump 315 of the section is connected to the second slurry pool 310; the first demister 303 is arranged above the desulfurization stage 302, and the first demister 303 is connected to the spraying section 304, and the spraying sec...
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