Yu-Qiu Cen, Shi-Hua Sang, Guo-Liang Nie, Chun-Tao Hu, Kuang-Yi Zhu
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引用次数: 0
Abstract
There are abundant lithium resources in seawater and brines. The thermodynamic phase equilibria of salt-water systems containing lithium have significant advantages to separation lithium from brines. Consequently, measurement and prediction of phase equilibria of LiCl–MClx (M = Na+, Mg2+, Sr2+)–H2O ternary systems are investigated at 298.2 K and 1 bar. The phase equilibria are determined using the isothermal dissolution equilibrium method and the solubilities of salts in the ternary systems are predicted using the Pitzer model. The predicted solubilities agree well with experimental data at 298.2 K and 1 bar.
Then, the changes of volume property () and compressibility () of three ternary mixed solutions at high pressure of 1–1000 bar were obtained in this work. The solubility product constants Ksp of salts at high pressure are calculated in detail. The thermodynamic prediction model of the phase equilibria is developed at high pressure of 1–1000 bar accordingly. The predicted phase equilibria at high pressure of 1–1000 bar are discussed and compared detailly.
海水和卤水中有丰富的锂资源。含锂盐水体系的热力学相平衡对于从卤水中分离锂具有显著优势。因此,研究了在 298.2 K 和 1 bar 条件下 LiCl-MClx (M = Na+、Mg2+、Sr2+)-H2O 三元体系相平衡的测量和预测。使用等温溶解平衡法确定了相平衡,并使用皮策模型预测了三元体系中盐类的溶解度。预测的溶解度与在 298.2 K 和 1 bar 条件下的实验数据吻合得很好。详细计算了高压下盐类的溶度积常数 Ksp。据此建立了 1-1000 bar 高压下相平衡的热力学预测模型。对预测的 1-1000 bar 高压下的相平衡进行了详细讨论和比较。
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