A kind of SNCR and SCR combined denitrification system and denitrification method of alumina roasting flue gas
A technology of alumina and aluminum hydroxide, applied in the field of SNCR and SCR combined denitration system, can solve the problems of weak alkalinity of aluminum materials, no desulfurization facilities, general SNCR effect, etc., and achieve the effect of compact system structure and cost saving.
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Embodiment 1
[0043] A combined SNCR and SCR denitrification system for alumina roasting flue gas, such as figure 1 As shown, it includes a roasting furnace, a three-stage cyclone separator, a second-stage cyclone separator, a first-stage cyclone separator and a dust collector connected in sequence; the roasting furnace is provided with an alumina material inlet, and the three-stage cyclone separator and A dry aluminum hydroxide inlet is set between the secondary cyclone separator, a wet aluminum hydroxide inlet is set between the secondary cyclone separator and the primary cyclone separator, and an oxidation A primary SNCR device and a secondary SNCR device are arranged sequentially in the flow direction of the aluminum roasting flue gas, the primary SNCR device is connected to the organic amine compound supply device; the secondary SNCR device is connected to the ammonia supply device; the secondary cyclone An SCR device is installed between the separator and the wet aluminum hydroxide in...
Embodiment 2
[0052] A combined SNCR and SCR denitrification system for alumina roasting flue gas, comprising a roasting furnace, a three-stage cyclone separator, a secondary cyclone separator, a primary cyclone separator and a dust collector connected in sequence; the roasting furnace is provided with an oxidation Aluminum material inlet, a dry aluminum hydroxide inlet is set between the third-stage cyclone separator and the second-stage cyclone separator, and a wet aluminum hydroxide inlet is arranged between the second-stage cyclone separator and the first-stage cyclone separator. Between the roasting furnace and the three-stage cyclone separator, a primary SNCR device and a secondary SNCR device are sequentially arranged along the flow direction of the alumina roasting flue gas, and the primary SNCR device is connected to the organic amine compound supply device; the secondary SNCR device The device is connected to the first ammonia supply device; an SCR device is arranged between the se...
Embodiment 3
[0063] Using the SNCR and SCR combined denitrification system and denitrification method described in Example 1, the 500,000 tons / year alumina roaster was denitrated. In flue gas, the concentration of NOx is 500mg / m 3 , spray methylamine at the outlet of the roaster, the initial molar ratio of methylamine to flue gas NOx is 0.05:1, spray ammonia water at the entrance of the three-stage cyclone separator, and the initial molar ratio of ammonia to flue gas after gasification is 0.7 : 1, the reaction temperature of primary SNCR and secondary SNCR is 990°C, the reaction temperature of SCR is 350°C, and the NOx concentration at the flue gas outlet of alumina roasting is lower than 50mg / m 3 , The escape ammonia concentration in the tail gas is lower than 1ppm.
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