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A coal chemical looping combustion mercury removal device and method

A technology of chemical looping combustion and mercury removal, which is applied in chemical instruments and methods, separation methods, and separation of dispersed particles. Effect of collection efficiency, increased contact time, and low cost

Active Publication Date: 2022-01-28
UNIV OF SHANGHAI FOR SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since the metal oxygen carrier in the fuel reactor is continuously reduced during the process of providing the required oxygen for coal combustion, its oxidizing ability is continuously weakened, so it is difficult to continue to oxidize the elemental mercury in the flue gas in the high temperature environment of the fuel reactor , and if more metal oxide oxygen carriers are fed into the fuel reactor in order to improve the mercury removal efficiency, it will bring problems such as increased costs due to the increase in the amount of metal oxygen carriers

Method used

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  • A coal chemical looping combustion mercury removal device and method
  • A coal chemical looping combustion mercury removal device and method
  • A coal chemical looping combustion mercury removal device and method

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Embodiment Construction

[0024] In order to make the technical means and effects realized by the present invention easy to understand, the present invention will be described in detail below in conjunction with the embodiments and accompanying drawings.

[0025] figure 1 It is a structural schematic diagram of a coal chemical looping combustion mercury removal device in the embodiment.

[0026] Such as figure 1 As shown, this embodiment provides a coal chemical looping combustion mercury removal device 100, including a fuel reactor 1, a fuel reactor U-phase valve 2, an air reactor 3, an air cyclone separator 4, and a flue gas cyclone separator 5 , air reactor U-phase valve 6, condenser 7, SCR denitration device 8, flue gas dust collector 9, wet flue gas desulfurization device 10 and CO 2 catcher 11.

[0027] The fuel reactor 1 is used to put fuel for burning.

[0028] The fuel reactor 1 is also provided with a fuel inlet 101 and a fuel air distribution plate 102 .

[0029] The fuel reactor U-phas...

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Abstract

The invention provides a coal chemical looping combustion mercury removal device, comprising: a fuel reactor; a U-phase valve of the fuel reactor connected to the fuel reactor; an air reactor connected to the U-phase valve of the fuel reactor; an air cyclone separator , connected to the air reactor; the flue gas cyclone separator, connected to the fuel reactor; the U-phase valve of the air reactor, connected to the air cyclone separator, the flue gas cyclone separator and the fuel reactor at the same time; the condenser, connected to the flue gas Cyclone separator connection; SCR denitrifier, connected to condenser; flue gas dust collector, connected to SCR denitrifier; wet flue gas desulfurizer, connected to flue gas dust collector; and CO 2 The collector is connected with the wet flue gas desulfurizer. The invention also provides a mercury removal method based on a coal chemical chain combustion mercury removal device to remove mercury from flue gas generated by combustion.

Description

technical field [0001] The invention belongs to the technical field of chemical looping combustion, and in particular relates to a coal chemical looping combustion mercury removal device and method. Background technique [0002] CO produced by industrial production and residential life 2 It is the main cause of global warming effect. for CO 2 In terms of emissions, chemical looping combustion is a method for CO 2 A new combustion technology for capture and storage. Compared with the traditional fuel combustion technology, the chemical looping combustion system consists of an air reactor and a fuel reactor. During the entire combustion process, there is no direct contact between the fuel and the air, and the oxygen required for fuel combustion is provided by the oxygen carrier. The specific process is as follows: the fuel entering the fuel reactor is burned under the action of the oxygen carrier, and the flue gas and fly ash produced by the combustion are separated after ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/86B01D53/64B01D53/62B01D53/46B01D45/12
CPCB01D53/8665B01D53/864B01D53/8671B01D45/12B01D2257/602B01D2257/502B01D2257/108B01D2258/0283
Inventor 刘敦禹刘壮金晶熊志波王秋麟程潜林黎明李伟冯亮倪明国蔡雨阳许开龙何军飞于志浩林丰李承绪黄小妞赵健沈翰郑良倩曲小珂
Owner UNIV OF SHANGHAI FOR SCI & TECH
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