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System and method for promoting coal fly ash to adsorb and remove pollutants such as mercury in flue gas

A technology for pollutants and fly ash, which is applied in the field of pollutant adsorption and removal systems, can solve the problems of secondary release, high operating cost of adsorption and mercury removal technology, and the impact of comprehensive utilization of fly ash, and achieves good adsorption and removal of mercury. The effect of reducing usage

Pending Publication Date: 2017-06-16
HUANENG CLEAN ENERGY RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0011] In order to meet the requirements of the global Minamata Convention and my country's relevant emission standards, protect the environment and the health and safety of the people, it is imperative to achieve efficient and low-cost mercury pollution control in coal-fired power plants. Among the current major coal-fired power plant-specific mercury removal technologies, Oxidative mercury removal technology has problems such as secondary release of mercury absorbed by the wet desulfurization system into flue gas or the environment. Adsorption mercury removal technology has disadvantages such as high operating costs and possible impact on the comprehensive utilization of fly ash.

Method used

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  • System and method for promoting coal fly ash to adsorb and remove pollutants such as mercury in flue gas
  • System and method for promoting coal fly ash to adsorb and remove pollutants such as mercury in flue gas
  • System and method for promoting coal fly ash to adsorb and remove pollutants such as mercury in flue gas

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Effect test

Embodiment 1

[0035] Such as figure 1 As shown, in this embodiment, a cyclone separator 8 is added at the entrance of the original dust collector 13 in the coal-fired power plant, and the residence time of fly ash in the flue gas is increased through the cyclone separator 8 . At the entrance of the cyclone separator 8, a flue gas cooler 6 is provided for reducing the temperature of the flue gas and recycling the working medium 12 which has absorbed the heat of the flue gas. At the same time, the cyclone separator 8 is used to capture the large particle size fly ash with a high carbon content > 80 μm, and a part of the large particle size fly ash is sent back to the inlet flue of the cyclone separator 8 through the fly ash conveying system 10 7. Another part of fly ash with large particle size enters the fly ash bin 9.

[0036] The characteristics of this embodiment are: it is not combined with oxidative mercury removal technology and activated carbon adsorption mercury removal technology, ...

Embodiment 2

[0038] Such as figure 2 As shown, in this embodiment, a cyclone separator 8 is added at the entrance of the original dust collector 13 in the coal-fired power plant, and the residence time of fly ash in the flue gas is increased through the cyclone separator 8 . At the entrance of the cyclone separator 8, a flue gas cooler 6 is provided for reducing the temperature of the flue gas and recycling the working medium 12 which has absorbed the heat of the flue gas. At the same time, the cyclone separator 8 is used to capture the large particle size fly ash with a high carbon content > 80 μm, and a part of the large particle size fly ash is sent back to the inlet flue of the cyclone separator 8 through the fly ash conveying system 10 7. Another part of fly ash with large particle size enters the fly ash bin 9.

[0039] The forced oxidant 2 and the catalytic oxidant 3 are used to increase the proportion of gaseous divalent mercury in the flue gas, and the gaseous divalent mercury i...

Embodiment 3

[0042] Such as image 3 As shown, in this embodiment, a cyclone separator 8 is added at the entrance of the original dust collector 13 in the coal-fired power plant, and the residence time of fly ash in the flue gas is increased through the cyclone separator 8 . At the same time, the cyclone separator 8 is used to capture the large particle size fly ash with a high carbon content > 150 μm, and a part of the large particle size fly ash is sent back to the inlet flue of the cyclone separator 8 through the fly ash conveying system 10 7. Another part of fly ash with large particle size enters the fly ash bin 9.

[0043] A certain amount of activated carbon is added into the fly ash conveying system 10 through the activated carbon bin 11, and the activated carbon is sent back to the outlet flue 5 of the air preheater 4 together with the large particle size fly ash. The particle size of the activated carbon used is 200 μm, so that most of the activated carbon used can also be captu...

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Abstract

The invention discloses a system and a method for promoting coal fly ash to adsorb and remove pollutants such as mercury in flue gas. The adsorbing and removing effects of the fly ash on the mercury are effectively improved by taking measures of reducing the temperature of the flue gas, prolonging the adsorption retention time of the fly ash, screening the fly ash with high mercury adsorbing capability, increasing the concentration of the fly ash with high mercury adsorbing capability and the like; on the basis, the method and the system can be further combined with an oxidation mercury removal technology and / or adsorption mercury removal technology, the defects in the prior art are overcome and efficiency mercury removal is realized; in addition, a good effect on control of other pollutants such as SO3 in the flue gas is achieved; and therefore, the method and the system have wide applicability, and the requirements of different coal-fired power plants on the pollutants such as mercury in the flue gas can be met.

Description

technical field [0001] The invention belongs to the technical field of thermal power generating units and environmental protection, and in particular relates to a system and method for promoting the adsorption and removal of mercury and other pollutants in flue gas by coal-burning fly ash. Background technique [0002] Mercury is a highly toxic substance that will cause long-term and serious harm to the environment and human body. As a trace element in coal, mercury is mostly discharged into the atmosphere along with flue gas during coal combustion. Although the mass concentration of mercury in the flue gas of coal-fired power plants is very low, only about 1-20 μg / m 3 , but its total amount is huge, and it is one of the most important sources of anthropogenic mercury emissions in the world. my country is the world's largest coal-burning country, so the problem of mercury emissions caused by coal burning is even more serious. [0003] Under the active promotion of the Uni...

Claims

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Application Information

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IPC IPC(8): B01D53/06B01D53/24B01D53/64B01D53/86B01D45/16F23J15/02F23J15/06
CPCB01D45/16B01D53/06B01D53/24B01D53/64B01D53/8665F23J15/006F23J15/02F23J15/027F23J15/06B01D2253/102B01D2253/10B01D2257/302B01D2258/0283B01D2257/602
Inventor 钟犁肖平江建忠吕海生
Owner HUANENG CLEAN ENERGY RES INST
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