The increasing global demand for lithium, driven by the rapid expansion of electric vehicles and energy storage systems, underlines the need for efficient lithium recovery technologies. This study explored the potential of using the fractional-submerged membrane distillation crystallizer (F-SMDC) process for recovering lithium carbonate (Li2CO3) crystals from high-salinity solutions. The F-SMDC integrates membrane distillation and cooling crystallization processes within a single reactor, utilizing concentration gradient (CG) and temperature gradient (TG) to enhance water recovery and resource crystallization. We investigated the behaviors of Li2CO3 crystallization, CG, and TG in presence of sodium sulfate (Na2SO4). Our results indicated that the low temperature-sensitive solubility of Li2CO3 is the current challenge for CG generation, as Li2CO3 crystallization tends to occur at the top of the reactor (at higher temperatures). Addition of Na2SO4 facilitated CG generation, improving the overall performance of the F-SMDC process for Li2CO3 crystallization at the bottom of the reactor. However, issues such as Li2CO3 crystal deposition on the membrane surface, changes in the CG tendency, and flux stabilization timing were observed. Thus, although F-SMDC shows promise for Li2CO3 recovery from high-salinity solutions, further process optimization is necessary to address the challenges of Li2CO3 crystallization and membrane fouling. Potential integration of additional crystallization techniques could enhance selectivity and recovery efficiency.
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