Boiler coal feeding method and system
A boiler and coal feeding technology, which is applied in the direction of combustion method, supply configuration, lighting and heating equipment, etc., can solve the problems of unguaranteed equipment, personal safety, economical operation of the boiler, loose coordination and control of units, difficulties in storage and combustion, etc. Achieve the effects of eliminating flammable and explosive materials, reducing the power consumption rate of pulverizing, and improving the efficiency of the unit
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Embodiment 1
[0045] see Figure 2 to Figure 5 As shown, a kind of method for feeding coal (powder) to a boiler provided in this embodiment, the boiler is a low-rank coal boiler, and the low-rank coal in this embodiment is taken as an example of lignite, which includes the following steps: first, the lignite is dried and extracted Quality, obtain pulverized coal; The method that lignite is carried out drying and upgrading is: produce hot gas flow (flue gas) with a kind of gas heating device (common as hot blast stove), the temperature is 200-1500 degree centigrade (the present embodiment is 901 degree Celsius), the hot air flow with oxygen content less than 10% is introduced in the cavity of drying device from air inlet 6, and the tail end of air outlet 8 is provided with induced draft fan (not shown in the figure), makes the cavity of drying device produce 100- 6000Pa (this embodiment is 4000Pa) negative pressure, the flow rate of hot air in the cavity is 8-14m / s (this embodiment is 10m / s)...
Embodiment 2
[0057] This embodiment provides a method for feeding coal (powder) to a boiler. The difference from Embodiment 1 is that the temperature of the hot air at the air inlet is 1000 degrees Celsius, the oxygen content is less than 8%, and the negative pressure of the drying device is 4500 Pa. The flow velocity of the medium-heat air is 10m / s; the rotating speed of the rotating device is 200 rpm, and the drying time of the lignite in the whole cavity is 3s. see Figure 6 As shown, the cavity of the drying device in this embodiment is divided into a plurality of chambers divided by the baffle plate 11. When the lignite is depolymerized and sprinkled in the chamber by the lifting teeth, the depolymerized lignite will flow with the hot air in the chamber. After drying in the chamber (mass and heat exchange), it will gradually flow to the next chamber, and finally be discharged through the discharge port. The baffle plate 11 is arranged on the bottom of the casing 3 or on the frame 2 ....
Embodiment 3
[0061] This embodiment provides a method for feeding coal (powder) to a boiler. The difference from Embodiment 1 is that the temperature of the hot air at the air inlet is 1200 degrees Celsius, the oxygen content is less than 8%, and the negative pressure of the drying device is 4000 Pa. The flow velocity of the medium-heat air is 10m / s; the rotating speed of the rotating device is 200 rpm, and the drying time of the lignite in the whole cavity is 3s. see Figure 7 As shown, the cavity of the drying device is divided into multiple chambers divided by staggered material baffles 11 and wind baffles 12, so that the direction of the hot air flow and lignite in the chamber is S-shaped, and the mass and heat exchange is sufficient. , thermal efficiency is improved. Thermal flow direction curve 10 such as Figure 7As shown, the material baffle 11 is arranged at the bottom of the casing 3, and the windshield 12 is arranged at the top of the casing. Parts that are the same as those ...
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Abstract
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