An ultra-low emission circulating fluidized bed boiler with three-stage desulfurization system
A circulating fluidized bed and desulfurization system technology, applied in chemical instruments and methods, separation methods, dispersed particle separation, etc., can solve the problems of poor quality fly ash that cannot be comprehensively utilized, fly ash that cannot be comprehensively utilized, and limited scope of application. Achieve the effects of high utilization rate of desulfurizer, convenient operation and control, and small transformation workload
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Embodiment 1
[0041] like figure 1 Shown is a newly built 300MW class circulating fluidized bed boiler with a three-stage desulfurization system. The combustion temperature of the boiler is 900°C, and the desulfurization agent addition system A in front of the furnace uses limestone particles with a median diameter of 3mm. District 7. The desulfurizer conveying system B in the furnace conveys limestone powder with a median diameter of 0.5 mm from the return pipe 15 to the dense-phase zone 7 of the furnace. The desulfurized flue gas in the furnace is cooled to 100°C by the exhaust gas temperature desuperheater 24, and then sent to the deep flue gas desulfurization system C for deep desulfurization. The desulfurization agent used in the deep flue gas desulfurization system C is slaked lime. The reducing agent nozzle 20 sprays the aqueous urea solution to the inlet flue 11 of the separator to further reduce the emission concentration of nitrogen oxides on the basis of the low-nitrogen combus...
Embodiment 2
[0044] A newly built 135MW circulating fluidized bed boiler with a three-stage desulfurization system. The combustion temperature of the boiler is 935°C. The desulfurization agent addition system A in front of the furnace uses limestone particles with a median diameter of 2mm, and the desulfurizer delivery system B in the furnace uses limestone powder with a median diameter of 0.3mm. A desulfurizer is also added to improve the desulfurization efficiency. The total amount of 3% sodium chloride desulfurization enhancer reduces the decomposition rate of calcium sulfate during combustion and improves the desulfurization efficiency.
Embodiment 3
[0046] A modified 200MW circulating fluidized bed boiler. The boiler was originally equipped with a desulfurization agent delivery system B in the furnace. A pre-furnace desulfurization agent addition system A and a deep flue gas desulfurization system C were added to the boiler. Through three-stage desulfurization The final sulfur dioxide emission concentration of the boiler is lower than 100mg / m 3 .
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