Converging type limekiln
A lime kiln and confluence flow technology, applied in lime production and other directions, can solve the problems of inability to simultaneously calcine large-grained and small-grained limestone materials, uneven heating of limestone, and large gas resistance of stone materials, so as to save equipment investment and avoid overheating. Burning and raw burning, the effect of complete heat utilization
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Embodiment 1
[0021] Confluence type lime kiln according to the present invention such as figure 1 As shown, it is mainly composed of a rectangular kiln body 15, a feed system, a discharge system, a combustion system, an air supply system and an exhaust gas discharge system. bring. The feed system includes feed conveyor, hopper 1 and feed lock 2, the discharge system includes discharge lock 13 and discharge conveyor, etc., the combustion system includes fuel pipelines and burners 9, and the air supply system includes blower 11 and Each control valve and the exhaust gas discharge system include a dust collector 5 , an induced draft fan 4 and a chimney 3 . The upper part of the kiln body is divided into three parts by two partition walls 17, the two outer cavities are coarse material bins 6, the middle cavity is a fine material bin 7, and the width of the coarse material bin is the fine material bin. 1.5 times the bin width. The kiln walls of the coarse material bins on both sides of the c...
Embodiment 2
[0024] Another embodiment of the present invention is as figure 2 As shown, this scheme is an improvement on the basis of Example 1. The kiln wall and the sub-fluid 10 of the two cooling bins 14 are provided with air holes, and the air holes on the kiln wall communicate with the gas collection device 22, and the gas collection device Connect the outlet of blower 11 through four-way valve 12. A feed lock 20 is provided in the middle of the cooling bins 14 on both sides. Other structures are the same as in Embodiment 1.
[0025] The operation mode of the cooling zone is that by controlling the action of the material lock 20 and the four-way valve 12, the cooling air enters the kiln body alternately from both sides. When the cooling air enters the left side cooling silo through the four-way valve 12, the other way is closed, the material lock 20 of the left side cooling silo is closed, and the material lock of the right side cooling silo is opened. The air enters the left coo...
Embodiment 3
[0027] The third embodiment of the present invention is as image 3 As shown, the calcining belts of the coarse-grain bins on both sides are respectively provided with two rows of burners 9, each row of 15 burners, the burners are solid fuel burners, and the fuel used is coal. The kiln wall with two cooling bins 14 and the sub-fluid 10 are provided with air holes, the air holes on the kiln wall communicate with the gas collecting device 22, and the gas collecting device is connected to the outlet of the blower 11 through a three-way valve 19f. The coarse grain bins on both sides of the calcination zone are provided with combustion air inlets 21, and the gas collectors 22 of the cooling bins on both sides of the cooling zone are connected to the combustion air inlets of the calcination zone through three-way valves 19d and 19c.
[0028] The operation process of this embodiment is that the cooling air enters the cooling silo on the left side from the air blower 11 to cool the li...
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Abstract
Description
Claims
Application Information
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