Production process of active lime
A production process and a technology for active lime, applied in the field of active lime preparation, can solve the problems affecting the quality of low-carbon and high-active lime, the process of treating little sulfur element, and the difficulty in discharging gas, and achieve the advantages of promoting industrialization and reducing raw burning. and overburning phenomenon, the effect of accelerated decomposition
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Embodiment 1
[0034] A kind of production technology of active lime, comprises the following steps:
[0035] (1) Limestone screening and pre-treatment: select limestone raw materials with an average diameter of 500 mm, clean and crush the limestone raw materials, and then screen to obtain limestone powder with an average diameter of 2 mm.
[0036] (2) Mixing: the limestone powder obtained in step (1) is uniformly mixed with 3% NaCl and 0.1% carbon with an average particle diameter of 2 μm to obtain a mixed limestone powder.
[0037] (3) Preheating: transport the mixed limestone powder obtained in step (2) to the preheater for preheating to 650°C for 20 minutes, and then transport the preheated mixed limestone powder to the first decompression chamber Reduced pressure to 0.3MPa.
[0038] (4) Calcination: The mixed limestone powder after decompression and preheating in step (3) is transferred to the sleeve lime kiln for calcination and heat preservation, and the gas consumption of the lower ...
Embodiment 2
[0043] A kind of production technology of activated lime, different from embodiment one is:
[0044] (1) In the step (1), the average diameter of the limestone raw material is 600 mm, and the average diameter of the limestone powder obtained after screening is 4 mm.
[0045] (2) The additive used in the step (2) is KCl, and the addition amount is 2.3%; the carbon average particle size is 1 μm, and the addition amount is 0.13%.
[0046] (3) In step (3), the preheating temperature is 750°C, and the preheating time is 13 minutes. The preheated mixed limestone powder is transported to the second decompression chamber for decompression to 0.7MPa, and then the second decompression chamber The mixed limestone powder in the bin is transported to the first decompression bin for decompression to 0.4MPa.
[0047] (4) In step (4), the gas consumption of the lower combustion chamber in the sleeve lime kiln is controlled to be 4 times the gas consumption of the upper combustion chamber; th...
Embodiment 3
[0052] A kind of production technology of activated lime, different from embodiment one is:
[0053] (1) In the step (1), the average diameter of the limestone raw material is 450 mm, and the average diameter of the limestone powder obtained after screening is 3 mm.
[0054] (2) The additive used in the step (2) is potassium oxalate, the addition amount is 2%; the carbon average particle size is 3 μm, the addition amount is 0.2%.
[0055] (3) In step (3), the preheating temperature is 680° C., and the preheating time is 10 minutes. The preheated mixed limestone powder is transported to the first decompression chamber for decompression to 0.5 MPa.
[0056] (4) In step (4), the gas consumption of the lower combustion chamber in the sleeve lime kiln is controlled to be 3 times the gas consumption of the upper combustion chamber; the excess air coefficient for the upper row of burners is 1.5. The calcination temperature is 900° C., and the calcination time is 4 minutes.
[0057]...
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