A method for producing xonotlite and alumina by hydrothermal method of fly ash alkali leaching and sintering
A technology of tobermorite and fly ash is applied in the field of comprehensive utilization of fly ash, which can solve the problems of scarcity, large resource and environmental impact, high production energy consumption and cost, and achieve engineering stability, land saving, etc. The effect of resources
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Embodiment 1
[0039] 1. Chemical beneficiation: Put the fly ash into the batching tank with chemical beneficiation solvent for batching. The chemical beneficiation solvent contains Na 2 O30g / L, containing SiO 2 ≤5g / L; the proportion of ingredients is 3 according to the weight ratio of chemical beneficiation solvent and fly ash; and then undergo chemical beneficiation treatment with a reaction temperature of 70°C and a reaction time of 600 minutes; 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%;
[0040] 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
[0053] Method is with embodiment 1, and difference is:
[0054] (1) The chemical beneficiation solvent contains Na 2 O80g / L, containing SiO 2 ≤5g / 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 100min; the washed filter residue is washed again to make fly ash with a water weight content of 40% Concentrate;
[0055] Na in the obtained crude sodium silicate solution 2 O concentration is 80g / L, SiO 2 The concentration is 40g / L;
[0056] (2) Na in sodium aluminate solution 2 o k The concentration is 210g / L, Na 2 O+K 2 O and Al 2 o 3 The molar ratio is 2.8, the mixing ratio of fly ash concentrate and sodium aluminate solution is based on the Na in all materials 2 O+K 2 O and Al 2 o 3 The molar ratio is 1.58, the leaching temperature is 270°C, and the reaction time is 60min; 2 o k The concentration is contro...
Embodiment 3
[0065] Method is with embodiment 1, and difference is:
[0066] (1) The chemical beneficiation solvent contains Na 2 O120g / L; the proportion of ingredients is 9 according to the weight ratio of chemical beneficiation solvent to fly ash; then chemical beneficiation treatment, the reaction temperature is 120°C, and the reaction time is 30min; the washed filter residue is washed again to make a powder with a water weight content of 45%. coal ash concentrate;
[0067] Na in the obtained crude sodium silicate solution 2 O concentration is 120g / L, SiO 2 The concentration is 60g / L;
[0068] (2) Na in sodium aluminate solution 2 o k The concentration is 245g / L, Na 2 O+K 2 O and Al 2 o 3 The molar ratio is 3.2, the mixing ratio of fly ash concentrate and sodium aluminate solution is based on the Na in all materials 2 O+K 2 O and Al 2 o 3 The molar ratio is 1.6, the leaching temperature is 280°C, and the reaction time is 30min; 2 o k The concentration is controlled at 165...
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