A method for producing tobermorite 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, and can solve the problems of large production energy consumption and cost, large resource and environmental impact, consumption and the like
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Embodiment 1
[0040] 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%;
[0041] 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
[0054] Method is with embodiment 1, and difference is:
[0055] (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 to fly ash; then chemical beneficiation treatment, the reaction temperature is 90°C, and the reaction time is 200min; the washed filter residue is washed again to make water with a weight content of 40%. fly ash concentrate;
[0056] Na in the obtained crude sodium silicate solution 2 O concentration is 80g / L, SiO 2 The concentration is 40g / L;
[0057] (2) Na in sodium aluminate solution 2 o k The concentration is 220g / 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 con...
Embodiment 3
[0066] Method is with embodiment 1, and difference is:
[0067] (1) The chemical beneficiation solvent contains Na 2 O120g / L, containing SiO 2 ≤5g / L; the proportion of ingredients is 9 according to the weight ratio of chemical beneficiation solvent and fly ash; then chemical beneficiation treatment, the reaction temperature is 120°C, and the reaction time is 30 minutes; the washed filter residue is washed again to make water with a weight content of 45%. fly ash concentrate;
[0068] Na in the obtained crude sodium silicate solution 2 O concentration is 120g / L, SiO 2 The concentration is 60g / L;
[0069] (2) Na in sodium aluminate solution 2 o k The concentration is 45g / 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 ...
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