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Deep denitration combustion method for tangential boiler

A combustion method and boiler technology, applied in the direction of combustion method, use of multiple fuels, combustion types, etc., can solve problems such as limited scope of application, ammonia escape, high requirements for boiler working conditions, etc., achieve wide applicability, reduce nitrogen Oxygen emission value, effect of reducing denitrification cost

Active Publication Date: 2017-01-04
SHANGHAI JIAO TONG UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

And because it is arranged after the exhaust air, if too much ammonia is injected, it will also cause ammonia to escape, so the requirements for the working conditions of the boiler are relatively high, and the scope of application is limited

Method used

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  • Deep denitration combustion method for tangential boiler
  • Deep denitration combustion method for tangential boiler
  • Deep denitration combustion method for tangential boiler

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] Such as figure 1 , figure 2 , image 3 As shown, the furnace of the tangential boiler is divided from bottom to top into the main combustion zone 1, the reduction zone 2 and the burnout zone 3. The four burners 4 are arranged in four corners, and each burner 4 is provided with several cross-arranged longitudinally The primary air nozzles 5 and the secondary air nozzles 6 are provided with a layer of reduction inhibitor nozzles 7 at the four corners of the furnace wall between the primary air nozzles 5 and the secondary air nozzles 6. The reduction inhibitor nozzles 7 at the four corners form a tangential circle. The tail flue behind the boiler air preheater is connected to all reduction inhibitor nozzles 7 through pipeline 8 and fan 9; the burn-out wind box 10 in the burn-out zone is provided with four-layer burn-out air nozzles 11; The tangential boiler deep denitrification combustion method is to send coal to the main combustion zone 1 of the furnace through the primar...

Embodiment 2

[0038] Such as Figure 4 As shown, the difference between this embodiment and the first embodiment is that the four-corner reduction inhibitor nozzles 7 are arranged in the primary air nozzles 5 or the secondary air nozzles 6 of each burner, and the reduction inhibitor nozzles 7 have a smaller caliber than The diameter of the primary air nozzle 5 or the diameter of the secondary air nozzle 6; the amino reduction inhibitor is sprayed from the reduction inhibitor nozzle 7 provided in the primary air nozzle 5 or the secondary air nozzle 6 in a manner of forming an imaginary tangent circle In; Since the caliber of the reduction inhibitor nozzle 7 is smaller than the caliber of the primary air nozzle 5 or the caliber of the secondary air nozzle 6, it does not affect the original primary air or secondary air injected into the furnace, which can achieve the same as the first embodiment Technical effect

Embodiment 3

[0040] Such as Figure 5 , Image 6 As shown, the difference between this embodiment and the first embodiment is only: the reduction inhibitor nozzle 7 is set on the four furnace walls of the reduction zone 2 between the main combustion zone 1 and the burnout zone 3; each furnace wall is provided with Two reduction inhibitor nozzles 7; the amino reduction inhibitor is sprayed from the two reduction inhibitor nozzles 7 on each furnace wall into the furnace in an imaginary tangent circle; the diameter of the reduction inhibitor nozzle 7 is 1-10mm , The opening is fan-shaped, the opening angle is between 10°~150°, the injection speed of the amino reduction inhibitor is between 10m / s~400m / s, the deflection angle of the reduction inhibitor nozzle 7 can be adjusted to adjust the diameter of the circle And the direction of rotation to meet the needs of different working conditions, and can achieve basically the same technical effect as the first embodiment;

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Abstract

The invention discloses a deep denitration combustion method for a tangential boiler. The hearth of the tangential boiler comprises a main combustion zone, a reduction zone and a burning-out zone; fuel coal is fed into the main combustion zone of the hearth for combustion through primary air in one or more layers of primary air nozzles; one or more layers of secondary air is introduced through secondary air nozzles in the main combustion zone; and one or more layers of burning-out air is introduced through burning-out air nozzles in the burning-out zone. The deep denitration combustion method is characterized in that an excess air coefficient in the main combustion zone ranges from 0.5 to 1.05, and the fuel coal is subjected to low oxygen combustion; an excess air coefficient in the burning-out zone ranges from 1.05 to 1.3, and the fuel coal is subjected to oxygen-enriched combustion; an amidogen reduction inhibitor is sprayed in through one or more layers of reduction inhibitor nozzles in the hearth below the burning-out air on the uppermost layer; the reduction inhibitor nozzles on the same layer are located on the same plane; and nitric oxides in smoke are reduced in a high-temperature environment in the furnace, and generation of new nitric oxides is inhibited. By adopting the deep denitration combustion method, a nitric oxide emission value at the outlet of the hearth can be obviously lowered, and ultra-low emission is realized; strict temperature windows and analysts are not needed; denitration cost is greatly lowered; combustion efficiency can also be ensured; economic benefit is obvious; and the deep denitration combustion method has wide applicability.

Description

Technical field [0001] The invention relates to a combustion method for denitration in a tangential boiler. Background technique [0002] A tangential boiler is a four-corner arrangement of burners, and coal is injected to form a tangential combustion method; the coal emits nitrogen oxides (NOx) pollutants during the combustion process, which can cause photochemical smog pollution, which will affect the human respiratory system and The survival of animals and plants will cause serious harm. my country’s latest "Emission Standard of Air Pollutants for Thermal Power Plants" (GB 13223-2011) stipulates that from January 1, 2015, all coal-fired boilers nitrogen oxides (in NO 2 Calculated) The emission limit is 100mg / Nm 3 (For the W-shaped flame furnace, the existing circulating fluidized bed thermal power boiler and the thermal power boiler completed and put into operation before December 31, 2003, the limit is 200 mg / Nm 3 ). [0003] At present, the denitration technologies that are m...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F23C5/32F23C7/02F23C9/00F23J7/00
CPCF23C5/32F23C7/02F23C9/00F23J7/00F23J2215/10Y02E20/34
Inventor 范卫东陈灿王勇刘泰生邓仲勇谢佳马晓伟吴明州
Owner SHANGHAI JIAO TONG UNIV
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