Aragonite type crystal seeds and aragonite type light calcium carbonate and preparation method thereof
A light calcium carbonate and aragonite-type technology, applied in calcium carbonate/strontium/barium, chemical instruments and methods, calcium/strontium/barium compounds, etc., can solve the problem of low solid content of calcium hydroxide, complex post-treatment process, Low production efficiency and other issues, to achieve the effect of stable product quality, low production cost, and industrialized production
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Embodiment 1
[0038] The automatic mechanical vertical steel kiln is adopted, the limestone with a size of 30-60mm is selected, the content of magnesium oxide is 0.5%, the ratio of coal to stone is 80kg / T limestone, the calcination temperature is controlled between 1000°C and the calcination time is 25h.
[0039] Lime is digested in hot water at 80°C, and the mass ratio of lime to water is 1:6. Add water to the digested rough pulp to adjust the concentration to 12%, first pass through a 100-mesh sieve, and then pass through a hydrocyclone to remove impurities to obtain a fine pulp. The temperature of the fine pulp is controlled at 45°C.
[0040] Pour the fine slurry into a carbonization tower, add phosphoric acid with a relative dry weight of 4% of calcium hydroxide, 0.5% sodium dihydrogen phosphate, and 0.5% sodium hexametaphosphate as crystal form control agents, and stir evenly.
[0041] Ventilate for carbonization, the kiln gas concentration is 30%, and the end point of carbonization ne...
Embodiment 2
[0045] The automatic mechanical vertical steel kiln is adopted, the limestone with a size of 30-60mm is selected, the content of magnesium oxide is 1.5%, the ratio of coal to rock is 80kg / T limestone, the calcination temperature is controlled between 1000°C and the calcination time is 25h.
[0046] Lime is digested in hot water at 80°C, and the mass ratio of lime to water is 1:6. Add water to the digested coarse pulp to adjust the concentration to 12%, first pass through a 100-mesh sieve, and then pass through a hydrocyclone to remove impurities to obtain a fine pulp. The temperature of the fine pulp is controlled at 50°C.
[0047] Pour the refined slurry into a carbonization tower, add phosphoric acid with a relative calcium hydroxide equivalent dry weight of 4.5%, 0.5% sodium dihydrogen phosphate, and 1.0% sodium hexametaphosphate as crystal form control agents, and stir evenly.
[0048] Ventilate for carbonization, the kiln gas concentration is 30%, and the end point of car...
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