Method for producing xonotlite and aluminum oxide according to coal ash sintering hydrothermal method
A technology of xonotlite and fly ash, which is applied in the field of comprehensive utilization of fly ash, can solve the problems of large consumption of limestone, large tailings, and difficulty in utilization, and achieve the effect of saving land and other resources and stabilizing engineering
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Embodiment 1
[0033] 1. Chemical beneficiation: Put the fly ash into the batching tank with chemical beneficiation solvent for batching. The chemical beneficiation solvent contains Na 2 O 30g / L, containing SiO 2 ≤5g / L; the proportion of ingredients is 3 according to the weight ratio of chemical beneficiation solvent and fly ash; then chemical beneficiation treatment is carried out, the reaction temperature is 70°C, and the reaction time is 600min; the obtained chemical beneficiation slurry is continuously separated and separated by a horizontal belt filter Washing to obtain the washed filter residue and crude sodium silicate solution; washing the washed filter residue again to make a fly ash concentrate with a water weight content of 30%;
[0034] Na in the obtained crude sodium silicate solution 2 O concentration is 30g / L, SiO 2 The concentration is 15g / L; the crude sodium silicate solution is refined by leaf filtration to obtain a refined sodium silicate solution with solid floating ma...
Embodiment 2
[0044] Method is with embodiment 1, and difference is:
[0045] (1) The chemical beneficiation solvent contains Na 2 O 80g / L; the proportion of ingredients is 6 according to the weight ratio of chemical beneficiation solvent and fly ash; the reaction temperature of chemical beneficiation treatment is 90°C, and the reaction time is 200min; the washed filter residue is washed again to make fly ash with a water weight content of 40% Concentrate;
[0046] Na in the obtained crude sodium silicate solution 2 O concentration is 80g / L, SiO 2 The concentration is 40g / L;
[0047] (2) The preparation ratio of the raw slurry is based on the main CaO and SiO in the raw slurry 2 The mol ratio is 2.00; The ratio of the total alkali moles and the total aluminum-iron moles is 0.95, and the weight content of water in the raw slurry is 40%;
[0048] (3) Send the raw slurry into the clinker sintering kiln for sintering by using a slurry pump with an outlet pressure of 4.0MPa through the spra...
Embodiment 3
[0054] Method is with embodiment 1, and difference is:
[0055] (1) The chemical beneficiation solvent contains Na 2 O 120g / L; the proportion of ingredients is 9 according to the weight ratio of chemical beneficiation solvent and fly ash; the reaction temperature of chemical beneficiation treatment is 120°C, and the reaction time is 30min; the washed filter residue is washed again to make fly ash with a water weight content of 45% Concentrate;
[0056] Na in the obtained crude sodium silicate solution 2 O concentration is 120g / L, SiO 2 The concentration is 60g / L;
[0057] (2) The preparation ratio of the raw slurry is based on the main CaO and SiO in the raw slurry 2 The molar ratio is 2.05; the ratio of total alkali moles and total aluminum-iron moles is 1.1, and the weight content of water in the raw slurry is 45%;
[0058] (3) Send the raw slurry into the clinker sintering kiln for sintering by using a slurry pump with an outlet pressure of 5.0MPa through the spray gun...
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