摘要
The feasibility of simultaneous water recovery, salt separation and effective descaling of hypersaline brine was investigated by diisopropylamine (DIPA)-based directional solvent extraction (DSE), using diluted/concentrated seawater with initial saline concentration range of 12–237 g/L at extraction temperatures of 5 and 15 °C, respectively. The water recovery shows an obvious boundary at saline concentration of 115 g/L under dual effect of specific water extraction efficiency and extraction cycles. High Cl − ion concentration in product water is in sharp contrast to the nearly complete removal of SO 4 2− and hardness ions, indicating that DIPA-based DSE process indeed achieved efficient separation and purification of Cl − ion from hypersaline brines. Especially, the radical precipitation of Mg 2+ and Ca 2+ ions in form of Mg(OH) 2 and CaCO 3 demonstrates effective descaling potential, although it leads to more DIPA residues in dewatered raffinate than product water. Moreover, an exponential correlation between the Cl − removal efficiency and specific water extraction efficiency further reveals the intrinsic relationship of water extraction process and transfer of Cl − ion to the product water. Overall, the study provides a novel approach for integrating the water recovery and separation of Cl − ion from ultra-high-salinity brines with radical precipitation of Mg 2+ and Ca 2+ ions in one step.
危险品化学品经营许可证(带存储)