Emission reduction and device for NOx generated in sintering process
A technology of sintering process and conveying equipment, which is applied in the field of sintering emission reduction, can solve the problems of no process, no NOx emission reduction modification, treatment, etc., and achieve the effect of convenient implementation and reduction of NOx emission
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Embodiment 1
[0030] In this embodiment, the mass ratio of coke powder 1 to coke powder 2 is 1:1, the mass ratio of lime 1 to lime 2 is 1:9, the mass ratio of coke powder 2 to lime 2 is 4:1, and the mass ratio of coke powder 1 and lime 2 is 1:1. The total mass of coke powder 2: the total mass of lime 1 and lime 2: the mass of limestone: the mass of dolomite: the mass of mixed ore: the mass of returned ore = 4:5:2:6:60:23. The residence time of the blend prepared in step (1) in the second mixing is 180s, that is, the second mixing granulation time is 240s, and the residence time of the spherical mixture prepared in step (2) in the secondary cylinder mixer for 30s. Finally, it is desintered together with the rest of the materials, and the NOx emission during the sintering process is 180mg / m 3 .
Embodiment 2
[0031] Embodiment 2: In this embodiment, the mass ratio of coke powder 1 to coke powder 2 is 0:1, the mass ratio of lime 1 to lime 2 is 1:9, and the mass ratio of coke powder 2 to lime 2 is 8:1. Total mass of coke powder 1 and coke powder 2: total mass of limestone 1 and limestone 2: mass of limestone: mass of dolomite: mass of mixed ore: mass of returned ore = 4:5:2:6:60:23. The second mixing granulation time is 20s. Finally, it is desintered together with the rest of the materials, and the NOx emission during the sintering process is 160mg / m 3 .
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