Lignite boiler combustion method capable of reducing nitrogen oxide emission
A nitrogen oxide and boiler combustion technology, which is applied in the field of boiler combustion of lignite, can solve the problems of high operating cost, low denitrification efficiency, and easy slagging of lignite, and achieves the effect of simple structure and high operation reliability
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specific Embodiment approach 1
[0014] Specific implementation mode one: combine figure 1 The combustion method of the lignite boiler that can reduce nitrogen oxide emissions in this embodiment adopts the lignite boiler that is divided into the main combustion zone 1 and the burnout zone 2 from bottom to top in the furnace, and the combustion zone between the main combustion zone 1 and the burnout zone 2 is The exhaust air nozzle 4 is the boundary; during the lignite combustion process, the amino reducing agent is sprayed into the main combustion zone 1, the burnout zone 2 and the horizontal flue 6 after atomization; the excess air coefficient of the main combustion zone 1 is controlled by air distribution to 0.9~ 1. The excess air ratio in the burnout zone 2 is 1.15 to 1.2; the NH produced by the amino reducing agent injected into the main combustion zone 1 3 The molar ratio of nitrogen oxides in flue gas in main combustion zone 1 is 0.5 to 1.1:1; NH 3 The molar ratio to the total nitrogen oxides in the fl...
specific Embodiment approach 2
[0016] Embodiment 2: The difference between this embodiment and Embodiment 1 is that the amino reducing agent is injected in three stages, and the first-stage amino reducing agent is injected from the primary reducing agent nozzle or the secondary air nozzle of the burner 3. The main combustion zone 1, the second-level amino reducing agent is sprayed into the burnout zone 2 from the burn-off air nozzle 4 and / or the furnace refraction angle nozzle 8, and the third-level amino reducing agent is injected into the horizontal through the amino reducing agent third-level nozzle 9 Flue 6. Other steps and parameters are the same as those in Embodiment 1.
specific Embodiment approach 3
[0017] Embodiment 3: The difference between this embodiment and Embodiment 1 or 2 is that the excess air coefficient in the main combustion zone 1 is controlled to 0.95 by air distribution, and the excess air coefficient in the burnout zone 2 is 1.16-1.17. Other steps and parameters are the same as those in Embodiment 1 or 2.
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