A temperature-resistance double-adjustable fluidizing air system for a circulating fluidized bed boiler
A circulating fluidized bed and air system technology, which is applied to fluidized bed combustion equipment, fuel burning in a molten state, lighting and heating equipment, etc. problems such as large impact, to achieve the effect of shortening start-up time, saving fuel, and ensuring stable operation
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Embodiment 1
[0047] figure 1 Shown is a 300MW CFB boiler. When the load is above 75%, the primary air rate is 60%, the corresponding bed temperature is 960°C, the primary hot air temperature is 230°C, and the resistance of the air distribution plate is 6.8kPa. for SO 2 The emission concentration is less than 200mg / m 3 , the calcium-sulfur molar ratio during operation was as high as 4.5. Through the primary hot air heat exchanger C, the primary hot air temperature is reduced to 170°C, the corresponding air distribution plate resistance is lowered to 5.2kPa, the temperature of the dense phase zone is lowered to 920°C, and the primary fan current is lowered by 45A. Under the same operating conditions, calcium sulfur SO can be achieved with a molar ratio as high as 2.8 2 The emission concentration is less than 200mg / m 3 , the effect of energy saving and emission reduction is remarkable.
[0048] In this application example, the air is pressurized and transported by the primary fan 13 to ...
Embodiment 2
[0052] figure 1 Shown is a 200MW CFB boiler. The boiler is equipped with a start-up burner. When running at 50% load in winter, the primary hot air temperature is 150°C, the resistance of the air distribution plate is only 1.6kPa, the air cap has serious slag leakage, the front and rear wall areas of the air distribution plate are poorly fluidized, and the bed surface appears many times. coke. The temperature of the primary hot air is raised to 200°C through the primary hot air heat exchanger C, and the heat exchange medium in the primary hot air heat exchanger C is the steam from the auxiliary steam header. After the temperature of the primary hot air increases, the resistance of the corresponding air distribution plate rises to 2kPa, the poor fluidization and the slag leakage of the air cap disappear, and the operation safety of the unit is improved.
Embodiment 3
[0054] figure 2 Shown is a 150MW CFB boiler. The boiler does not have a start-up burner, and can only be started through the bed oil gun, and the fuel consumption during the start-up process is high. During startup, the temperature of the fluidized air is increased from 50°C to 150°C by starting the primary hot air heat exchanger C. The heat exchange medium in the primary hot air heat exchanger C is the steam from the auxiliary steam header, and the startup time is shortened by about 2 hours. Significant savings in starting oil.
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