A method for producing wollastonite and alumina by hydrothermal method of fly ash alkali leaching and sintering
A technology of fly ash and wollastonite, which is applied in the field of comprehensive utilization of fly ash solid waste and mineral processing, and can solve the problems of great impact and scarcity of resources and the environment
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Embodiment 1
[0037] 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, the reaction temperature is 70°C, and the reaction time is 600 min; the obtained chemical beneficiation slurry is continuously separated through a horizontal belt filter and washing to obtain the washing filter residue and crude sodium silicate solution; the washing filter residue is washed again to make a fly ash concentrate with a water weight content of 45%;
[0038] 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 matter less than 1...
Embodiment 2
[0052]Method is with embodiment 1, and difference is:
[0053] (1) The chemical beneficiation solvent contains Na 2 O 90g / 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 100°C, and the reaction time is 200 min; the washed filter residue is washed again to make a powder with a water weight content of 40%. coal ash concentrate;
[0054] Na in the obtained crude sodium silicate solution 2 O concentration is 80g / L, SiO 2 The concentration is 30g / L;
[0055] (2) Na in sodium aluminate solution 2 O 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 1.56, the leaching temperature is 265°C, and the reaction time is 60min; 2 The O concentration is controlled at 145g / L; the de...
Embodiment 3
[0065] Method is with embodiment 1, and difference is:
[0066] (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 pulverized coal with a water weight content of 30% 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 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 The O concentration is controlled at 165g / L; the d...
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