Phase Equilibria of Dicalcium Silicate in HCL and NaOH-NaAl (OH)4-Na2CO3 Aqueous Solutions Using The Bromley-Zemaitis Model

- Organization:
- Canadian Institute of Mining, Metallurgy and Petroleum
- Pages:
- 14
- File Size:
- 1491 KB
- Publication Date:
- Jan 1, 2014
Abstract
The behavior of dicalcium silicate in NaOH-NaAl(OH)4-Na2CO3 solution is of significance for controlling the silica level in the production of alumina via the sintering process. Dicalcium silicate samples were obtained through a twostep approach: coprecipitation of calcium and silicate from CaCl2-Na2SiO3-NaOH solutions; and calcination of the hydrated precursor at 1200°C for 4 hours. The optimization of the synthesis parameters including temperature, solution concentrations and aging time was also investigated. Xray diffraction (XRD) and chemical analysis show that the calcined solids include dicalcium silicate with trace amounts of wollastonite. The solubility of the synthesized dicalcium silicate in HCl, NaOH, mixed NaOH-NaAl(OH)4 and NaOH-NaAl(OH)4-Na2CO3 solutions was determined. It was found that the solubility increases with increasing HCl and NaOH concentration. The effect of temperature on the solubility in HCl solutions is limited, but the solubility decreases with increasing temperature in NaOH solutions. The solubility of dicalcium silicate in NaOH-NaAl(OH)4 and NaOH-NaAl(OH)4-Na2CO3 solutions was shown to increase with increased temperature, Al(OH)3 and Na2CO3 concentration. The BromleyZemaitis model for the aqueous electrolyte system was selected to predict the solubility of dicalcium silicate. The model’s predictions yielded certain success compared with experimental solubility data.
Citation
APA:
(2014) Phase Equilibria of Dicalcium Silicate in HCL and NaOH-NaAl (OH)4-Na2CO3 Aqueous Solutions Using The Bromley-Zemaitis ModelMLA: Phase Equilibria of Dicalcium Silicate in HCL and NaOH-NaAl (OH)4-Na2CO3 Aqueous Solutions Using The Bromley-Zemaitis Model. Canadian Institute of Mining, Metallurgy and Petroleum, 2014.