Cement kiln flue gas waste heat utilization and purification system and low-temperature SCR denitration system
A flue gas waste heat and purification system technology, applied in the field of low-temperature SCR denitrification system
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Embodiment 1
[0038] Adopt the technical solution of the embodiment of the waste heat utilization and purification system of the cement kiln flue gas, wherein the cement kiln 1 is a cement kiln without an SNCR denitrification system in the furnace. During the operation of the system, the state of the dust-removed flue gas output by the dust collector 6 is: the concentration of nitrogen oxides is 300mg / Nm 3 Around, dust concentration 3 , gas volume is about 5000Nm 3 / h, the temperature is 100-150°C. The low-temperature SCR denitrification system controls the volume ratio of ammonia to nitrogen oxides to be 1.05. The denitrification efficiency of the low-temperature SCR denitrification system was measured > 80%, and the outlet NO x Concentration3 , dust concentration 3 .
Embodiment 2
[0040] Adopt the technical solution of the embodiment of the cement kiln flue gas waste heat utilization and purification system, wherein the cement kiln 1 is a cement kiln equipped with an SNCR denitrification system in the furnace. During the operation of the system, the state of the dust-removed flue gas output by the dust collector 6 is: the concentration of nitrogen oxides is 260mg / Nm 3 Around, dust concentration 3 , gas volume is about 5000Nm 3 / h, the temperature is 100-150°C. The volume ratio of ammonia to nitrogen oxides set by the SNCR denitrification system in the furnace is 1.5-1.7:1, and the volume ratio of ammonia to nitrogen oxides set by the low-temperature SCR denitrification system is 0.9-1.05:1 . The denitrification efficiency of the low-temperature SCR denitrification system was measured > 85%, and the outlet NO x Concentration3 , dust concentration 3 .
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