A method for producing tobermorite and alumina by fly ash sintering hydrothermal method
A technology of tobermelite and fly ash, which is applied in the field of comprehensive utilization of fly ash, and can solve problems such as consumption, large impact on resources and the environment, and shortage
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Embodiment 1
[0038] 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; 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%;
[0039] 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 matt...
Embodiment 2
[0050] Method is with embodiment 1, and difference is:
[0051] (1) The chemical beneficiation solvent contains Na 2O80g / 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 concentrate with a water weight content of 40% mine;
[0052] Na in the obtained crude sodium silicate solution 2 O concentration is 80g / L, SiO 2 Concentration is 40g / L;
[0053] (2) Raw slurry preparation ratio is based on the main CaO and SiO in the raw slurry 2 The molar ratio of is 2.00, and the ratio of total alkali molar number and total aluminum-iron molar number is 0.95, and the weight content of water in raw slurry is 40%;
[0054] (3) Send the raw slurry into the clinker sintering kiln for sintering by using a slurry pump with an outlet pressure of 3.0MPa through the spray...
Embodiment 3
[0060] Method is with embodiment 1, and difference is:
[0061] (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 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 concentrate with a water weight content of 45% mine;
[0062] Na in the obtained crude sodium silicate solution 2 O concentration is 20g / L, SiO 2 The concentration is 60g / L;
[0063] (2) Raw slurry preparation ratio is based on the main CaO and SiO in the raw slurry 2 The molar ratio of is 2.05, and the ratio of total alkali molar number and total aluminum-iron molar number is 1.1, and the weight content of water in raw slurry is 45%;
[0064] (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 ...
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