Desulfurization and denitrification device and method for sintering flue gas
A technology for sintering flue gas, desulfurization and denitrification, which is applied in the direction of combined devices, separation methods, chemical instruments and methods, etc., can solve the problems of high equipment investment and operation costs, cost problems, and lack of flue gas, and achieve high desulfurization and denitrification efficiency. The effect of simple process flow and simple process structure
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Embodiment 1
[0054] The content of pollutants, dust and water vapor in the initial sintering flue gas is: SO 2 -1105mg / Nm 3 , NO x -450mg / Nm 3 , Dust-8305mg / Nm 3 , H 2 O-9.5% (volume content), flue gas temperature 160°C.
[0055] according to figure 1 , the sintering flue gas first passes through the flue gas dust removal system 1, the dust removal system is composed of three electrostatic precipitators, and the dust content in the flue gas after dust removal is 12mg / Nm 3 , the flue gas temperature is 151°C; then, the flue gas enters the desulfurization reactor 2, and the dust content in the flue gas after activated coke desulfurization is 5mg / Nm 3 , SO 2 The content is 13mg / Nm 3 , H 2 The O content is 2.1% by volume, and the flue gas temperature is reduced to 123°C; then, the flue gas enters the flue gas pipeline after being discharged from the desulfurization reactor 2, and flows into the flue gas pipeline from the ammonia system 8 before entering the denitrification reactor 3 ...
Embodiment 2
[0058] The content of pollutants, dust and water vapor in the initial sintering flue gas is: SO 2 -1210mg / Nm 3 , NO x -410mg / Nm 3 , Dust-10560mg / Nm 3 , H 2 O-9.1% (volume content), flue gas temperature 172°C.
[0059] according to figure 1 , the sintering flue gas first passes through the flue gas dust removal system 1. The dust removal system consists of three electrostatic precipitators and a high temperature bag filter. The dust content in the flue gas after dust removal is 10mg / Nm 3 , the flue gas temperature is 146°C; then, the flue gas enters the desulfurization reactor 2, and the dust content in the flue gas after activated coke desulfurization is 4mg / Nm 3 , SO 2 The content is 16mg / Nm 3 , H 2 The O content is 1.8% by volume, and the temperature of the flue gas is reduced to 117°C; then, the flue gas enters the flue gas pipeline after being discharged from the desulfurization reactor 2, and flows into the flue gas pipeline from the ammonia system 8 before enter...
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