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An oxygen-enriched combustion boiler system and its operating method

An oxygen-enriched combustion and boiler technology, applied in the direction of combustion methods, separation methods, and controlled combustion, to achieve the effects of achieving performance and economic benefits, ensuring continuous and safe operation, and optimal performance and economic benefits

Active Publication Date: 2022-04-12
CHINA SHENHUA ENERGY CO LTD +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Aiming at the above problems in the prior art, the present invention proposes an oxygen-enriched combustion boiler system and its operation method, which solves the problem of excessive oxygen content in the circulating flue gas existing in the existing oxygen-enriched combustion boiler system The technical problems caused by deflagration and tempering

Method used

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  • An oxygen-enriched combustion boiler system and its operating method
  • An oxygen-enriched combustion boiler system and its operating method
  • An oxygen-enriched combustion boiler system and its operating method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] This example uses figure 1 As shown in the boiler system structure, the flue gas outlet of the boiler furnace is sequentially connected with the flue gas purification treatment device 9, the secondary fan 2, the first oxygen injector 3 for the secondary air, the second oxygen injector 4 for the secondary air and the The burners 5 are connected in sequence, and the boiler flue gas is used as the source of the secondary air. The first oxygen injector 3 for the secondary air is set between the flue gas outlet of the secondary fan 2 and the boiler furnace, and is set close to the boiler furnace. The secondary air The second oxygen injector 4 is arranged close to the burner 5, and the distance between the second oxygen injector 4 of the secondary air and the burner 5 is 1.8 times the flue gas outlet connecting pipeline diameter of the second oxygen injector 4 of the secondary air . The purification treatment device 9 includes a dust collector and a desulfurization tower.

...

Embodiment 2

[0052] This example uses figure 2 As shown in the boiler system structure, the flue gas outlet of the boiler furnace is connected to the flue gas purification treatment device 9 through a pipeline. Connect with the secondary fan 2, the first oxygen injector 3 for the secondary air, the second oxygen injector 4 for the secondary air and the burner 5 through a branch, and the outlet of the flue gas purification treatment device 9 is connected with the exhaust gas through another branch. The primary fan 6, the coal mill 7, the primary air first oxygen injector 8, the primary air second oxygen injector 10 and the burner 5 are connected in sequence.

[0053] The secondary air second oxygen injector 4 is set close to the burner 5, and the distance between the secondary air second oxygen injector 4 and the burner 5 is 1.8 times the outlet connection pipeline of the secondary air second oxygen injector 4 diameter.

[0054] The primary air first oxygen injector 8 is arranged between...

Embodiment 3

[0059] This example uses image 3 The structure of the boiler system shown is basically the same as that of the boiler system described in Embodiment 2, except that the system includes an oxygen pipeline M, one end of the oxygen pipeline M is connected to the burner 5, and the oxygen pipeline M The other end is connected to the oxygen storage tank, the first oxygen injector 3 for the secondary air, the second oxygen injector 4 for the secondary air, the first oxygen injector 8 for the primary air, and the second oxygen injector 10 for the primary air pass through the oxygen injection pipeline M1 to M4 are respectively connected to the oxygen pipeline M, and an oxygen regulating valve is set on the oxygen injection pipeline.

[0060] When the boiler system is in normal operation or an accident occurs, the first oxygen injector 3 for secondary air, the second oxygen injector 4 for secondary air, the first oxygen injector 8 for primary air, and the second oxygen injector 10 for p...

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Abstract

The invention discloses an oxygen-enriched combustion boiler system and its operation method, comprising a boiler furnace, a burner arranged on the boiler furnace, a first air blower, a first oxygen injector, and a second oxygen injector, wherein the boiler The flue gas outlet of the furnace is sequentially connected with the first blower, the first oxygen injector, the second oxygen injector and the burner, and the second oxygen injector is arranged near the burner location. The system and operation method of the invention solve the technical problem of backfire in the air supply pipeline in the oxygen-enriched combustion system, ensure the continuous and safe operation of the oxygen-enriched combustion system, and realize the best performance and economic benefits.

Description

technical field [0001] The invention relates to the technical field of thermal energy engineering, in particular to an oxygen-enriched combustion boiler system and an operating method. Background technique [0002] Oxygen-enriched combustion is based on the existing coal-fired power generation technology, using high-purity oxygen to replace combustion-supporting air, and at the same time using flue gas circulation to adjust the combustion and heat transfer characteristics of the boiler, which can obtain high-concentration CO-rich 2 Flue gas, through further condensation and compression purification, can easily realize large-scale CO 2 enrichment and reduction. [0003] During the heating process, pulverized coal will undergo pyrolysis to produce flammable gases such as methane. In the oxygen-enriched combustion system, the gas supply method of flue gas circulation is adopted. When the boiler furnace is turned off, due to the pulverized coal and heat entering the furnace Th...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): F23B80/02F23J15/02F23L1/00F23L5/02F23L7/00F23L9/00F23L15/00F23L17/00F23N3/00F23N5/26B01D53/26
CPCF23B80/02F23L5/02F23L7/007F23L15/00F23L1/00F23L9/00F23L17/00F23J15/022F23J15/02B01D53/265F23N3/007F23N5/26F23N2231/28F23N2235/02Y02E20/34
Inventor 吴海波傅培舫陈威男廖海燕柳朝晖余学海张翼陈创社郑楚光
Owner CHINA SHENHUA ENERGY CO LTD