Combustor capable of reducing soot emission and combustion method
A combustion method and burner technology, applied in the direction of combustion method, solid fuel combustion, combustion equipment, etc., can solve the problems that the burner cannot meet the actual application requirements, limit the energy utilization of biomass fuel, and lack of combustion technology, etc., to achieve Increase the effect of self-priming, increase strength, and improve combustion efficiency
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Embodiment 1
[0036] This embodiment provides a burner and a combustion method for reducing soot emissions, figure 1 It is a schematic structural view of the burner of the present invention, including the burner body 6 body, the side wall of the burner body 6 is connected with a feeding mechanism, and an additional speaker is arranged on the side wall of the burner body 6 and below the feeding mechanism 4. The middle part of the burner body 6 is provided with a slag cleaning mechanism, and the lower part of the burner body 6 is provided with an ash collecting bucket a1, which is located in the support frame b17, and the support frame b17 is used to fix and support the burner body 6. It is connected with the bottom of the burner main body 6 and is used to place the ash hopper a1. The top of the burner body 6 is provided with an exhaust and dust removal mechanism, which can ensure sufficient oxygen supply, and can also filter out ash flocs produced during the combustion process to reduce poll...
Embodiment 2
[0048] The burner of this embodiment is basically the same as that described in Embodiment 1, the only difference being that the metal rolling net 5 with a mesh number of 30 is used, and the frequency of the loudspeaker 4: the frequency of the loudspeaker 4 is set to 200 Hz, and the amplitude is 150 Pa. The feed rate of biomass fuel was 300 g / min.
[0049] Similar to Example 1, the soot rate produced during the steady state combustion of the flame in the original state of the burner was measured, and the NOx and CO contents in the flue gas were tested to be 100ppm and 9201ppm respectively. After the pulse combustion started, the soot generation rate at the tail was measured, and the measured NOx and CO contents in the flue gas were 16ppm and 465ppm. Among them, the suppression efficiency of soot is 98.8%, and the suppression efficiency of NOx and CO is 84% and 95%.
Embodiment 3
[0051] The burner of this embodiment is basically the same as that described in Embodiment 1, the only difference being that the metal rolling net 5 with a mesh number of 10 is used, and the frequency of the loudspeaker 4: the frequency of the loudspeaker 4 is set to 80 Hz, and the amplitude is 100 Pa. The feed rate of biomass fuel was 200 g / min.
[0052] Similar to Example 1, the soot rate produced during the steady state combustion of the flame in the original state of the burner was measured, and the NOx and CO contents in the flue gas were tested to be 81ppm and 6250ppm respectively. After the pulse combustion started, the soot generation rate at the tail was measured, and the measured NOx and CO contents in the flue gas were 10ppm and 426ppm. Among them, the suppression efficiency of soot is 99%, and the suppression efficiency of NOx and CO is 87% and 93%.
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