The current study is focused on the thermodynamic modeling and experimental measurement of metal hydroxide precipitation titration curves for the single- and multi-component sulfate systems. The systematic analytical model is developed based on Bromley-Zemaitis's theory and H. E. Wirth's theory to accurately predict the precipitation behavior of sulfate systems under different operating conditions and to simulate the precipitation titration curve. The titration curves established using the analytical model are compared with the curves built using the numerical mixed-solvent electrolyte model provided in OLI software along with the experimental measurement. The results demonstrate a good agreement between the analytical model, numerical model, and experimental approach while unveiling the limitations of the developed analytical model such as the disregard of multi-species ions, constant solution density, and constant water activity. The effect of three key operating parameters, namely initial solution pH, initial metal ion concentration, and reaction temperature, on the precipitation behaviors is investigated with emphasis on the ion interaction, precipitation pH, the amount of precipitant required, and species equilibrium.
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