A method for preparing calcium silicate hydrate and magnetic hydrotalcite from industrial waste
A technology of magnetic hydrotalcite and hydrated calcium silicate, which is applied in chemical instruments and methods, hydrotalcite, solid waste removal, etc., can solve the problems of low added value, high cost, and low cost, and achieve high energy consumption Effect
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Embodiment 1
[0076] A method for preparing calcium silicate hydrate and magnetic hydrotalcite using industrial waste, the method is divided into five steps: step 1 is burning and activating white mud and high-sulfur coal; step 2 is distillation; step 3 is distillation extraction; step 4 is extraction and separation; Step 5 is synthesis and "three wastes" treatment;
[0077] Step 1: Combustion activation of white mud and high-sulfur coal
[0078] White mud and high-sulfur coal are mixed according to the ratio of calcium atom to aluminum atom in the ratio of 0.8:1-1.5:1, and sent to the fluidized combustion chamber (1-1-1) for combustion, and the soot produced during the combustion process enters the The lime mud gas-solid mixer (1-2-1) is mixed with the lime mud and returned to the fluidized combustion chamber (1-1-1) through the second fan (1-2-10); The ratio of calcium-aluminum substances in high-sulfur coal to white mud is 2:1-3:1.
[0079] The ash generated by combustion enters the se...
Embodiment 2
[0100] This embodiment is basically the same as the method for preparing calcium silicate hydrate and magnetic hydrotalcite by using industrial waste described in Example 1, the difference is that in step 1, white mud and high-sulfur coal are based on the amount of calcium atoms and aluminum atoms The ratio of the amount is 0.8:1-1.5:1 mixing ratio, preferably 1.4:1.
[0101] Calcium atoms and aluminum atoms are 1.4:1, reducing the amount of lime mud added through the mixer, which is conducive to keeping the temperature in the furnace stable.
Embodiment 3
[0103] This example is basically the same as the method described in Example 1 for preparing calcium silicate hydrate and magnetic hydrotalcite from industrial waste, except that in step 1, during the stable combustion process, high-sulfur coal and white mud are maintained. The ratio of the amount of medium-calcium-aluminum substances is 2:1-3:1; preferably 2.2:1.
[0104] The preferred ratio is 2.2:1, which can reduce the energy consumption during lime mud treatment.
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