Combined denitrification system and method for alumina baked fuel gas
A technology of alumina and flue gas, applied in chemical instruments and methods, combined devices, separation methods, etc., can solve the problems of ammonia escape and large influence of temperature window, and achieve the effect of reducing usage, reducing influence and reducing ammonia escape.
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[0029] A combined denitrification system for alumina roasting flue gas. Along the flue gas flow direction, the combined denitrification system includes a roasting kiln, a three-stage cyclone separator, a two-stage cyclone separator, a The first-stage cyclone separator and the terminal dust collector, the wet raw material drying inlet is provided between the second-stage cyclone separator and the first-stage cyclone separator, and the third-stage cyclone separator and the second-stage cyclone separator are provided. There is a semi-dry raw material drying inlet, and a dry raw material drying inlet is provided between the roasting kiln and the three-stage cyclone separator. There is a first purification gas inlet for the mixed gas of gas and alcohol organic matter, and a second purification gas inlet for introducing ozone is provided between the primary cyclone separator and the terminal dust collector.
[0030] The combined denitrification method using the above combined denitr...
Embodiment 1
[0040] According to the combined denitrification system and method in the above embodiments, this example selects an alumina roasting kiln with an annual output of about 500,000 tons for denitrification experimental research. In flue gas, NO x The concentration is 500mg / m 3 , spray 5% ammonia gas at the high temperature of the boiler (about 1000 ° C temperature section), and spray 2% methanol gas after gasification as an additive at the same time; add a concentration of 200mg / m at the low temperature of the boiler feed 3 of ozone. The results show that NO is produced at the flue gas outlet of the alumina roasting kiln x The concentration is reduced to 100mg / m 3 Below, the existence of escaped ammonia can hardly be detected in the exhaust gas at the same time.
Embodiment 2
[0042] According to the combined denitrification system and method in the above embodiments, this embodiment also selects an alumina roasting kiln with an annual output of about 500,000 tons for denitrification experimental research. NO in flue gas x The concentration is 500mg / m 3 , spray 5% ammonia gas at the high temperature of the boiler (about 1000 ° C temperature section), and spray 5% ethanol gas after gasification as an additive at the same time; add a concentration of 250mg / m at the low temperature of the boiler feed 3 of ozone. The results show that NO is produced at the flue gas outlet of the alumina roasting kiln x The concentration is reduced to 100mg / m 3 Below, the existence of escaped ammonia can hardly be detected in the exhaust gas at the same time.
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