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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

Active Publication Date: 2015-04-29
马鞍山雾净环境科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The purpose of this invention is to provide a relatively simple and practical system for reducing the content of particulate matter after flue gas desulfurization, so as to solve the problem that the outlet of the desulfurization system contains relatively large concentration of particulate matter

Method used

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  • Process and system for reducing particle content after flue gas desulfurization
  • Process and system for reducing particle content after flue gas desulfurization
  • Process and system for reducing particle content after flue gas desulfurization

Examples

Experimental program
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Effect test

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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Abstract

The invention provides a process and a system for reducing particle content after flue gas desulfurization. The system comprises a desulfurization tower and a second slurry pond; a first slurry pond is arranged at the bottom of the desulfurization tower; a flue gas inlet is formed in the lower part of the desulfurization tower; a desulfurization stage which is divided into at least two sections is positioned in the desulfurization tower and above the flue gas inlet; the front desulfurization stage section in contact with the flue gas is connected to a first slurry pond through a circulating pump at the first section, and the last desulfurization stage section is connected with the second slurry pond through the circulating pump at the second section; a first defogging device is arranged above the desulfurization stage and connected with a spray section; the spray section is connected with a second defogging device, and a flue gas outlet is formed in the upper part of the second defogging device. The system further comprises a third slurry pond which is connected with the spray section through a third circulating pump. The system is simple in structure; the engineering cost cannot be excessively increased in a new project or a reconstruction project; the content of fine particles in the exhausted flue gas can be obviously decreased, and thus the pollution of the desulfurization system to the surrounding environment can be avoided.

Description

technical field [0001] The invention belongs to the field of air pollutant control, and in particular relates to a process and a system capable of reducing the content of particulate matter in flue gas discharged from a wet desulfurization system. Background technique [0002] Wet desulfurization is currently the most mature technology and the most widely used flue gas desulfurization process. Limestone / lime-gypsum wet flue gas desulfurization technology accounts for about 85% of the FGD systems put into operation in the world. The desulfurization methods of generating units are limestone / lime-gypsum wet flue gas desulfurization, and the desulfurization efficiency can generally reach more than 95%. [0003] With the development of my country's economy and society, flue gas emissions are on the rise, causing environmental problems to become increasingly prominent. In order to protect the ecological environment and people's health, the corresponding pollutant control standards...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/80B01D53/50B01D53/73
Inventor 凌斌聂江宁
Owner 马鞍山雾净环境科技有限公司
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