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System and method for preparing filling paste based on magnesium slag/fly ash coupled flue gas desulfurization and carbon reduction treatment

A fly ash and carbon treatment technology, which is applied in gas treatment, separation methods, chemical instruments and methods, etc., can solve the problems of large proportion of desulfurization absorbent, limited resource utilization methods, large amount of gypsum, etc., and achieve comprehensive savings Operating cost, the effect of solving boiler flue gas emissions

Pending Publication Date: 2021-12-17
XIAN UNIV OF SCI & TECH +1
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Problems solved by technology

[0005] Although the limestone-gypsum wet desulfurization process is mature and widely used, there are still some problems: In the operating cost of limestone-gypsum wet flue gas desulfurization, the cost of electricity and desulfurization absorbent (limestone) accounts for a large proportion, exceeding the total operating cost of the desulfurization system 90% of
In addition, limestone mining has caused serious damage to the ecological environment of the mining area. The amount of gypsum produced by this method is relatively large, and resource utilization is limited. At present, a large proportion of desulfurized gypsum produced is disposed of as waste. This problem needs to be solved urgently
[0006] Therefore, at this stage, the coal-electricity integration project is facing three major problems: First, in order to improve the resource recovery rate and coal mining rate, coal mines use fully-mechanized coal mining to cause ground subsidence (collapse) in the mining area, damage to the ecological environment, and construction. (Structure) damage to buildings; secondly, when the mined coal is transformed into resources such as power generation, coal chemical industry, and magnesium smelting or deep-processed, the large industrial solid wastes such as fly ash, slag, magnesium slag, and gasification slag are produced. Proper disposal issues; third, the current air pollutant emissions require that the flue gas emissions of coal-fired boilers have low emissions, the limestone consumption of wet desulfurization, and the disposal of by-product desulfurization gypsum
However, under the current process system in which the steps of "coal mining-deep processing-waste treatment" are separated, it is difficult to properly solve the above problems

Method used

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  • System and method for preparing filling paste based on magnesium slag/fly ash coupled flue gas desulfurization and carbon reduction treatment

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Embodiment Construction

[0035] The implementation of the present invention will be described in detail below in conjunction with the drawings and examples.

[0036] The invention is a system for preparing filling paste based on magnesium slag / fly ash coupled flue gas desulfurization and carbon reduction treatment, wherein the magnesium slag can be derived from the Pidgeon method of magnesium smelting, that is, ferrosilicon reducing agent is used in the reduction tank to Industrial solid waste remaining after calcined dolomite is reduced to metallic magnesium.

[0037] Fly ash can come from coal-fired boiler fly ash / fine ash, that is, the fine ash collected from the flue gas of coal-fired boilers in thermal power stations and coal chemical production coal-fired boilers through dust collectors.

[0038] The present invention can also use other similar calcium oxide system materials to replace magnesium slag / fly ash.

[0039] In the present invention, flue gas generally refers to coal-fired boiler flue g...

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Abstract

A system for preparing filling paste based on magnesium slag / fly ash coupling flue gas desulfurization and carbon reduction treatment comprises: a flue gas desulfurization reactor, wherein the bottom of the flue gas desulfurization reactor is provided with a desulfurization slurry collection pool, the top of the flue gas desulfurization reactor is provided with a flue gas outlet, an absorption slurry distribution device is arranged below the flue gas outlet, a flue gas inlet is located above the desulfurization slurry collection pool and below the absorption slurry distribution device, and the flue gas inlet is connected with the flue gas discharge port of a coal-fired boiler dust remover; an absorption slurry preparation device used for preparing absorption slurry by utilizing magnesium slag and / or fly ash raw materials, wherein the absorption slurry is conveyed to the absorption slurry distribution device, and the absorption slurry is in contact with boiler flue gas to realize flue gas desulfurization and carbon reduction and is converted into desulfurization slurry which falls into the desulfurization slurry collection pool; a slurry concentration pool connected with the desulfurized slurry collection pool and used for reducing the water content of the desulfurized slurry to obtain concentrated slurry meeting the preparation requirements of the filling paste; and a filling paste preparation system used for preparing filling paste by using the concentrated slurry.

Description

technical field [0001] The invention belongs to the technical field of resource recycling of bulk industrial solid waste, and in particular relates to a system and method for preparing filling paste based on magnesium slag / fly ash coupled flue gas desulfurization and carbon reduction treatment. Background technique [0002] There are two types of coal mining: conventional mining and green filling mining. In conventional mining, there are common mechanized coal mining technology, comprehensive mechanized coal mining technology, blasting coal mining technology and so on. These mining methods have large output and high recovery rate, but in the process of mining, they will cause problems such as ground subsidence (collapse), ecological environment damage, and building (structure) damage. Filling mining is a green mining technology that is expected to break through the current conventional coal mining problems. [0003] According to the current standard of green coal mining, c...

Claims

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Application Information

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IPC IPC(8): C04B28/08C04B28/04B01D53/50B01D53/62B01D53/80
CPCC04B28/08C04B28/04B01D53/502B01D53/62B01D53/80B01D2257/504B01D2258/0283B01D2251/402B01D2251/404C04B2111/00724C04B18/08C04B7/02C04B18/10C04B22/062C04B22/145C04B22/10
Inventor 任武昂唐仁龙李龙清邵小平李超
Owner XIAN UNIV OF SCI & TECH
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