Multi-grade high-efficiency low-nitrogen combustion method and multi-grade high-efficiency low-nitrogen combustion system for circulating fluidized bed boiler

A circulating fluidized bed, low-nitrogen combustion technology, applied in fluidized bed combustion equipment, combustion methods, fuels burned in a molten state, etc., can solve the problem of increasing thermal nitrogen oxides, affecting the full combustion of fuel, slagging and high temperature Corrosion increase and other problems, to achieve the effect of reducing the formation of fuel-type nitrogen oxides and thermal-type nitrogen oxides, reducing the tendency of slagging and high-temperature corrosion in the furnace, and inhibiting the generation of thermal-type nitrogen oxides

Active Publication Date: 2014-02-26
武汉和信益科技有限公司
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Problems solved by technology

However, due to the unique low-temperature combustion and secondary air grading layout of the circulating fluidized bed boiler combustion technology, the nitrogen oxide generation is lower than that of ordinary pulverized coal boilers using the same fuel. Emission Standards of Air Pollutants "About Coal-fired Boilers 450-1100mg / Nm 3 Therefore, there are few researches and achievements on low-nitrogen combustion technology
However, the 2011 version of the emission standard raised the NOx emission limit for existing circulating fluidized bed boilers to 200mg / Nm 3 100mg / Nm is strictly enforced for new units 3 Therefore, the existing and new circulating fluidized bed boilers are faced with the problem of further reducing the amount of nitrogen oxides produced in the furnace
Especially for circulating fluidized bed boilers burning low-quality fuels with high volatile content and low ash melting point such as biomass, peat, oil shale, etc., there is a problem of uneven combustion and heat release of fuel along the furnace height direction, and the middle and lower parts of the furnace are generally There will be a relatively high combustion peak temperature, which increases the formation of thermal nitrogen oxides, and is also prone to slagging and high-temperature corrosion
[0005] In order to reduce the formation of nitrogen oxides, solutions are often adopted to reduce the combustion temperature in the furnace and increase the range of the reducing atmosphere in the furnace. However, this will affect the full combustion of fuel to a large extent, and will increase the mechanical capacity of the boiler. incomplete combustion loss
For circulating fluidized bed boilers that have already adopted air staged combustion technology, the greater the degree of air staging, the greater the degree of reduction of nitrogen oxides; however, as the degree of air staging increases, the furnace The larger the area in the reducing atmosphere, the greater the probability of slagging and high-temperature corrosion in these areas, the greater the carbon content of fly ash, which will affect the economical and safe operation of the boiler

Method used

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  • Multi-grade high-efficiency low-nitrogen combustion method and multi-grade high-efficiency low-nitrogen combustion system for circulating fluidized bed boiler
  • Multi-grade high-efficiency low-nitrogen combustion method and multi-grade high-efficiency low-nitrogen combustion system for circulating fluidized bed boiler
  • Multi-grade high-efficiency low-nitrogen combustion method and multi-grade high-efficiency low-nitrogen combustion system for circulating fluidized bed boiler

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] A high-temperature circulating fluidized bed boiler, multi-stage high-efficiency low-nitrogen combustion system including furnace, air distribution plate, primary air inlet and secondary air inlet, the furnace is divided into anoxic combustion zone, reduction zone, oxidation zone from bottom to top In the combustion zone and the burnout zone, the upper boundary of the oxygen-deficient combustion zone is 4.5 meters away from the surface of the air distribution plate, the upper boundary of the reduction zone is 7.5 meters away from the surface of the air distribution plate, and the upper boundary of the oxidation combustion zone is 9.5 meters away from the surface of the air distribution plate. The exclusion zone is located above the upper boundary of the oxidative combustion zone. There is a furnace bottom primary air inlet under the air distribution plate, a layer of reducing air inlets on the front and rear walls of the furnace in the reduction zone, and a layer of oxid...

Embodiment 2

[0034] In this embodiment, in a medium-temperature circulating fluidized bed boiler, the combustion air in the furnace is classified into the overall depth, along the height direction of the furnace, and according to the combustion characteristics of the fuel, the furnace is divided into oxygen-deficient from bottom to top. Combustion zone, reduction zone, oxidative combustion zone and burnout zone.

[0035] The combustion of fuel in the furnace and the generation and reduction process of nitrogen oxides are basically the same as in Example 1, the difference between the two is:

[0036] In this embodiment, in order to ensure the high-efficiency combustion of fuel, the height between the uppermost layer of the exhaust air inlet and the first row of tubes on the first set of convective heating surfaces on the upper part of the furnace is set as the average velocity of the flue gas in the burnout zone. 2.5 times.

[0037] In this embodiment, the reducing air, the oxidizing air a...

Embodiment 3

[0040] The general layout of this embodiment and embodiment 1, the combustion of fuel in the furnace and the generation and reduction process of nitrogen oxides are basically the same, the difference between the two is:

[0041] In this embodiment, an annular primary air inlet is provided on the furnace wall close to the top of the air distribution plate.

[0042] In this embodiment, the secondary air enters the furnace in four layers, namely two layers of reducing air, one layer of oxidizing air and one layer of exhausted air. Among them, the nozzles of the reducing air in the lower layer are located on the rear wall of the furnace, the nozzles of the reducing air in the upper layer are located in the front wall of the furnace; the nozzles of the oxidizing air are located on the walls on both sides of the furnace; the nozzles of the exhaust air are located on the four walls of the furnace.

[0043] In this embodiment, the excess air ratio in the oxygen-deficient combustion zo...

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Abstract

The invention relates to a multi-grade high-efficiency low-nitrogen combustion method and a multi-grade high-efficiency low-nitrogen combustion system for a circulating fluidized bed boiler. According to the method, combustion air enters a furnace hearth through corresponding inlets respectively to divide the furnace hearth into a less oxygen combustion area, a reduction area, an oxidative combustion area and a burning-out area; the excess air coefficients of each area are respectively controlled to be 0.55-0.95, 0.75-1.15, 1.05-1.25 and greater than or equal to 1.20, so that a fuel is dispersed and uniformly combusted in the furnace hearth. The burning-out area is positioned above the upper boundary of the oxidative combustion area and has the effective height which is not less than 2.5 times of a flue gas average velocity value in the area, the upper boundaries of the remaining areas are respectively 2.0-5.5 meters, 4.5-9.0 meters and 8.0-12.0 meters away from the surface of an air distribution plate. The system which is applicable to the method comprises the furnace hearth, the air distribution plate, a primary air inlet and a secondary air inlet; at least one layer of reducing air inlet, at least one layer of oxidative air inlet and at least one layer of burning-out air inlet are respectively formed in at least one wall of the corresponding area of the furnace hearth. By virtue of the method and the system, the generation capacity of nitrogen oxides can be reduced, and high-efficiency combustion of the fuel can also be realized.

Description

technical field [0001] The invention relates to a combustion method and a combustion system of a boiler, in particular to a multi-stage, high-efficiency, low-nitrogen combustion method and a combustion system of a circulating fluidized bed boiler. Background technique [0002] Nitrogen oxides are one of the main pollutants of atmospheric environmental pollution, which endanger human health, affect plant growth, and participate in the destruction of the ozone layer. [0003] Nitrogen oxides mainly come from the direct combustion of solid, liquid and gaseous fuels. As a major emitter of nitrogen oxides, the control of nitrogen oxides emissions from thermal power plants is very important. In recent years, the low-nitrogen combustion technology that controls the formation of nitrogen oxides during fuel combustion and the flue gas denitrification technology that reduces the formed nitrogen oxides have made great progress. [0004] Low-nitrogen combustion technology can greatly r...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F23C10/00F23C10/18F23C10/20F23L9/00
Inventor 陈勇
Owner 武汉和信益科技有限公司
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