Method and device for multi-grade mixed combustion of double fuels at cyclone state
A combustion device and dual-fuel technology, which is applied in the direction of gaseous fuel and powder fuel combustion, combustion equipment, lighting and heating equipment, etc., can solve the problem of unsatisfactory pulverized coal burnout effect, high NOx content in flue gas, and coal type adaptation Insufficient compatibility and other issues, to achieve the effects of easy access, reduced flue gas NOx emission concentration, and reasonable distribution
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specific Embodiment 1
[0040] The auxiliary fuel flow sprayed forward by the central nozzle (4) is the second-stage auxiliary fuel stream (11), and the auxiliary fuel in the second-stage auxiliary fuel stream (11) is the same as that in the first-stage auxiliary fuel jet (3). The components are the same, and they are injected from the center of the nozzle to the depth of the burner flame along the axis. When gaseous fuel is used as auxiliary fuel, the injection velocity of the second-stage auxiliary fuel ranges from 35 to 50m / s; when high-quality solid fuel is used as auxiliary fuel , the range of injection velocity is 25~35m / s. When the high-speed stream of the central auxiliary fuel moves forward rapidly in the center of the burner flame, the outer side of the stream contacts the high-temperature flue gas in the recirculation zone of the burner, and the fuel on the outer side of the high-speed stream is ignited to form a long strip-shaped torch, which can further stabilize the coal When most of th...
specific Embodiment 2
[0044] The auxiliary fuel supply method of this embodiment is suitable for gas auxiliary fuel, especially methane (CH 4 ) other than alkanes as the main components of gas fuels (such as liquefied petroleum gas, etc.) and gas fuels with methane as the main component and higher content of other alkanes (such as natural gas, etc.) are more effective. The composition of the first-stage and second-stage gas-assisted fuel is the same, and the supply ranges are 2-10% and 10-20% of the total calorific value of the burner fuel, respectively.
[0045] Specific implementation example three
specific Embodiment 3
[0047] When the central high-speed stream (11) and the outer ring high-speed stream (12) are injected into the depth of the burner flame, the second-stage auxiliary fuel on the outer surface of the high-speed stream (11) and (12) burns to form an inner and outer The distributed strip-shaped long torch can ensure good stability of the pulverized coal flame even when the load is low and the pulverized coal airflow presents general fluctuations.
[0048] This implementation example is applicable to the situation where gaseous fuel is used as auxiliary fuel, such as: coke oven gas, producer gas, natural gas, liquefied petroleum gas, blast furnace gas, converter gas, and combustible gas by-products produced in chemical industries. The composition of the first-stage and second-stage gas auxiliary fuels is the same, and the supply ranges are 2-10% and 10-25% of the total calorific value of the burner fuel, respectively. The auxiliary fuel provided by the outer ring high-speed stream (...
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