A low NOx combustion system for flue gas recirculation and ultra-fine pulverized coal staged gasification
A technology of flue gas recirculation and combustion system, applied in the direction of staged combustion, flue gas combustion, combustion type, etc., can solve the problem of high investment cost, achieve the effect of low investment cost, reduce oxygen content, and reduce NOX generation
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0031]The primary pulverized coal enters the gasification furnace 2 through the primary fuel gasification nozzle 3, and the excess air coefficient in the gasification furnace 2 is guaranteed to be 0.2 by adjusting the air volume and the recirculation flue gas volume; the secondary pulverized coal enters through the secondary fuel combustion nozzle 5 The combustion furnace 4, the circulating flue gas enters the combustion furnace 4 through the circulating flue gas nozzle 8, ensuring that the excess air ratio in the combustion furnace 4 is 0.9; the unburned reducing gas and coke rise into the burnout zone, and the burnout air is burnt out from the top The air nozzle 6 enters the burnout area, and is fully mixed and burned out; the flue gas after combustion enters the flue 7, and part of the flue gas enters the flue gas pipe 10 through the flue gas outlet 11 on the side wall of the flue 7, and then passes through the circulating flue gas nozzle 8 Enter the gasification furnace 2 a...
Embodiment 2
[0033] The primary pulverized coal enters the gasification furnace 2 through the primary fuel gasification nozzle 3, and the excess air coefficient in the gasification furnace 2 is guaranteed to be 0.3 by adjusting the air volume and the recirculation flue gas volume; the secondary pulverized coal enters through the secondary fuel combustion nozzle 5 The combustion furnace 4, the circulating flue gas enters the combustion furnace 4 through the circulating flue gas nozzle 8, ensuring that the excess air coefficient in the combustion furnace 4 is 0.85; the unburned reducing gas and coke rise into the burnout zone, and the burnout air is burnt out from the top The air nozzle 6 enters the burnout area, and is fully mixed and burned out; the flue gas after combustion enters the flue 7, and part of the flue gas enters the flue gas pipe 10 through the flue gas outlet 11 on the side wall of the flue 7, and then passes through the circulating flue gas nozzle 8 Enter the gasification fur...
Embodiment 3
[0035] The primary pulverized coal enters the gasification furnace 2 through the primary fuel gasification nozzle 3, and the excess air coefficient in the gasification furnace 2 is guaranteed to be 0.5 by adjusting the air volume and the recirculation flue gas volume; the secondary pulverized coal enters through the secondary fuel combustion nozzle 5 Combustion furnace 4, the circulating flue gas enters the combustion furnace 4 through the circulating flue gas nozzle 8, ensuring that the excess air ratio in the combustion furnace 4 is 0.8; the unburned reducing gas and coke rise into the burnout zone, and the burnout air is burnt out from the top The air nozzle 6 enters the burnout area, and is fully mixed and burned out; the flue gas after combustion enters the flue 7, and part of the flue gas enters the flue gas pipe 10 through the flue gas outlet 11 on the side wall of the flue 7, and then passes through the circulating flue gas nozzle 8 Enter the gasification furnace 2 and ...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 

