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
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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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