Preparation method of calcined kaolin with high whiteness and ultrahigh oil absorption
A technology for calcined kaolin and oil absorption, applied in chemical instruments and methods, inorganic chemistry, silicon compounds, etc., can solve the problems of low oil absorption and whiteness value, high oil absorption and low wear of calcined kaolin, so as to avoid repetition. The effect of sintering agglomeration, reducing the proportion, and bonding firmly
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Embodiment 1
[0025] A method for preparing calcined kaolin with high whiteness and ultra-high oil absorption, including removing impurities from coal gangue → batching → crushing → iron removal → dry grinding → light burning in a reducing atmosphere → crushing → slurry preparation → iron removal → wet grinding → slurry preparation → Iron removal→horizontal snail classification→disk classification→filtration dehydration→slurry→iron removal→drying→pre-disintegration and depolymerization→weak reducing atmosphere calcination→rapid cooling→post-disintegration and depolymerization→product;
[0026] Wherein, the coal gangue is silicon-aluminum type coal gangue, m(Al 2 o 3 ) / m(SiO 2 )=0.8, b value=2.5 after calcination;
[0027] In order to ensure the realization of calcined whiteness, product performance and batching uniformity, the loss on ignition of raw materials after the batching: 16.2%, calorific value: 40Kcal / Kg, Fe 2 o 3 and TiO 2 Total content <1.5%;
[0028] In order to control th...
Embodiment 2
[0034] A method for preparing calcined kaolin with high whiteness and ultra-high oil absorption, including removing impurities from coal gangue → batching → crushing → iron removal → dry grinding → light burning in a reducing atmosphere → crushing → slurry preparation → iron removal → wet grinding → slurry preparation → Iron removal→horizontal snail classification→disk classification→filtration dehydration→slurry→iron removal→drying→pre-disintegration and depolymerization→weak reducing atmosphere calcination→rapid cooling→post-disintegration and depolymerization→product;
[0035] Wherein, the coal gangue is silicon-aluminum type coal gangue, m(Al 2 o 3 ) / m(SiO 2 )=0.8, b value=2.4 after calcination;
[0036] In order to ensure the realization of calcined whiteness, product performance and batching uniformity, the loss on ignition of raw materials after the batching: 16.2%, calorific value: 40Kcal / Kg, Fe 2 o 3 and TiO 2 Total content <1.5%;
[0037] In order to control th...
Embodiment 3
[0043] A method for preparing calcined kaolin with high whiteness and ultra-high oil absorption, including removing impurities from coal gangue → batching → crushing → iron removal → dry grinding → light burning in a reducing atmosphere → crushing → slurry preparation → iron removal → wet grinding → slurry preparation → Iron removal→horizontal snail classification→disk classification→filtration dehydration→slurry→iron removal→drying→pre-disintegration and depolymerization→weak reducing atmosphere calcination→rapid cooling→post-disintegration and depolymerization→product;
[0044] Wherein, the coal gangue is silicon-aluminum type coal gangue, m(Al 2 o 3 ) / m(SiO 2 )=0.8, b value=2.5 after calcination;
[0045] In order to ensure the realization of calcined whiteness, product performance and batching uniformity, the loss on ignition of raw materials after the batching: 16.2%, calorific value: 40Kcal / Kg, Fe 2 o 3 and TiO 2 Total content <1.5%;
[0046] In order to control th...
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