A method for preparing multi-stage calcined kaolin by suspending calcination of coal series kaolin
A technology for calcining kaolin and coal series kaolin, which is applied to chemical instruments and methods, silicates, silicon compounds, etc., can solve problems such as low processing capacity and heat utilization efficiency, incomplete combustion of organic matter, and long calcination heat preservation time, etc., to achieve Effective recovery and utilization of heat energy, large processing capacity, low energy consumption and low cost
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Embodiment 1
[0040] Process such as figure 1 shown;
[0041] Coal series kaolin contains SiO by mass percentage 2 45.44%, Al 2 o 3 37.47%, Fe 2 o 3 0.17%, CaO0.33%, TiO 2 0.14%, MgO 0.11%, K 2 O 0.24%, Na 2 O 0.32%, C 0.91%; crush the coal series kaolin to a particle size ≤ 15mm, and then grind it to an average particle size of 0.002mm to make a powder;
[0042] The powder is continuously conveyed to the suspension dehydration calciner through the screw feeder; the bottom of the suspension dehydration calciner is equipped with a first burner and gas inlet, the top is equipped with a feed inlet, and the upper part is equipped with a discharge outlet and a first cyclone separator Connected; feed gas into the first burner, and feed air into the gas inlet of the suspension dehydration calciner, and start the flue gas generated by the first burner to enter the suspension dehydration calciner; the powder entering the suspension dehydration calciner is under the action of airflow It ...
Embodiment 2
[0051] Method is with embodiment 1, and difference is:
[0052] (1) Coal series kaolin contains SiO by mass percentage 2 42.19%, Al 2 o 3 38.32%, Fe 2 o 3 0.29%, CaO0.56%, TiO 2 0.37%, MgO 0.48%, K 2 O 0.29%, Na 2 O 0.19%, C 1.49%; powder average particle size 0.0022mm;
[0053] (2) Dehydration reaction is carried out at 250°C; the residence time of the powder in the suspension dehydration calciner is 6min;
[0054] (3) Dehydration reaction at 800°C; the residence time of the dehydrated material in the suspension dehydroxylation calciner is 20min;
[0055] (4) Decarburization reaction at 900°C; the volume flow ratio of air to nitrogen is 1:1.5; the residence time of the dehydroxylation material in the suspension decarburization calciner is 60min;
[0056] (5) The temperature of the decarbonized material drops to 200°C to form a cooling material; after the countercurrent heat exchange between the decarbonized material and air, the temperature of the hot air after h...
Embodiment 3
[0059] Method is with embodiment 1, and difference is:
[0060] (1) Coal series kaolin contains SiO by mass percentage 2 44.83%, Al 2 o 3 36.21%, Fe 2 o 3 0.22%, CaO0.48%, TiO 2 0.25%, MgO 0.34%, K 2 O 0.33%, Na 2 O 0.2%, C 1.18%; powder average particle size 0.0025mm;
[0061] (2) Dehydration reaction is carried out at 300°C; the residence time of the powder in the suspension dehydration calciner is 2min;
[0062] (3) Dehydration reaction at 900°C; the residence time of the dehydrated material in the suspension dehydroxylation calciner is 10 minutes;
[0063] (4) Decarburization reaction at 950°C; the volume flow ratio of air and nitrogen is 1:2; the residence time of the dehydroxylation material in the suspension decarburization calciner is 90min;
[0064] (5) The temperature of the decarbonized material drops to 250°C to form a cooling material; after the countercurrent heat exchange between the decarbonized material and the air, the temperature of the hot air ...
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