Method for preparing high-activity alpha type hemihydrate gypsum cementing materials by using reaction of chlorine-alkali waste liquid treating ardealite
A technology for waste liquid treatment and hemihydrate gypsum, which is applied in the production of gypsum cementitious materials, waste liquid resource utilization and environmental protection engineering fields, can solve the problems of low calcium chloride concentration, large steam consumption, waste of resources, etc. The effect of saving operating costs, saving resources and saving energy
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Embodiment 1
[0024] Calcium hydroxide in the form of milk of lime (250g calcium hydroxide / Kg milk of lime) and chlor-alkali waste liquid are continuously or almost continuously introduced into the reaction device according to the amount of 20Kg milk of lime / t chlor-alkali waste liquid, and are alkalized to remove chlor-alkali waste liquid Inorganic impurities such as magnesium ions and iron ions are precipitated in the waste liquid, and the reactant is in the reaction device for about 30 minutes, and the pH value of the mixed solution is 7.8. At this time, the molar concentration of inorganic ion impurities such as magnesium ions and iron ions in the solution is not Greater than 0.005 mol / L. After the reaction, the solution and products are continuously or almost continuously discharged from the reaction device, and the precipitation temperature is controlled at 65°C; the flocculant anionic polyacrylamide flocculant CAFFARO is added to the solution coming out of the reaction device, and the...
Embodiment 2
[0026] Calcium hydroxide in the form of milk of lime (250g calcium hydroxide / Kg milk of lime) and chlor-alkali waste liquid are continuously or almost continuously introduced into the reaction device according to the amount of 20Kg milk of lime / t chlor-alkali waste liquid, and are alkalized to remove chlor-alkali waste liquid Inorganic impurities such as magnesium ions and iron ions are precipitated in the waste liquid, and the reactants are in the reaction device for about 30 minutes, and the pH value of the mixed solution is 8.3. At this time, the molar concentration of inorganic ion impurities such as magnesium ions and iron ions in the solution is not Greater than 0.005 mol / L. After the reaction, the solution and products are continuously or almost continuously discharged from the reaction device, and the precipitation temperature is controlled at 60°C; the flocculant anionic polyacrylamide flocculant CAFFARO is added to the solution coming out of the reaction device, and t...
Embodiment 3
[0028]Calcium hydroxide in the form of milk of lime (250g calcium hydroxide / Kg milk of lime) and chlor-alkali waste liquid are continuously or almost continuously introduced into the reaction device according to the amount of 40Kg milk of lime / t chlor-alkali waste liquid, and alkalization is carried out to remove the chlor-alkali waste liquid Inorganic impurities such as magnesium ions and iron ions are precipitated in the waste liquid, and the reactant is in the reaction device for about 30 minutes, and the pH value of the mixed solution is 8.5. At this time, the molar concentration of inorganic ion impurities such as magnesium ions and iron ions in the solution is not Greater than 0.005 mol / L. After the reaction, the solution and products are continuously or almost continuously discharged from the reaction device, and the precipitation temperature is controlled at 45°C; the flocculant anionic polyacrylamide flocculant CAFFARO is added to the solution coming out of the reactio...
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