Work

Recovery of lithium carbonate crystals from a high salinity solution using membrane crystallizer with concentration and temperature gradients

Year: 2024

Type: article

Abstract: 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 (Li 2 CO 3 ) 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 Li 2 CO 3 crystallization, CG, and TG in presence of sodium sulfate (Na 2 SO 4 ). Our results indicated that the low temperature-sensitive solubility of Li 2 CO 3 is the current challenge for CG generation, as Li 2 CO 3 crystallization tends to occur at the top of the reactor (at higher temperatures). Addition of Na 2 SO 4 facilitated CG generation, improving the overall performance of the F-SMDC process for Li 2 CO 3 crystallization at the bottom of the reactor. However, issues such as Li 2 CO 3 crystal deposition on the membrane surface, changes in the CG tendency, and flux stabilization timing were observed. Thus, although F-SMDC shows promise for Li 2 CO 3 recovery from high-salinity solutions, further process optimization is necessary to address the challenges of Li 2 CO 3 crystallization and membrane fouling. Potential integration of additional crystallization techniques could enhance selectivity and recovery efficiency. • Fractional-submerged membrane distillation crystallizer is useful to recovery Li 2+ . • Concentration of feed influenced on the degree of concentration gradient. • Low solubility of Li 2 CO 3 at high temperatures cause membrane fouling. • Membrane reaction crystallization could develop the performance of F-SMDC.

Source: Desalination

DOI: 10.1016/j.desal.2024.118311

Authors: Youngkwon Choi, Linitho Suu, Joowan Lim, June-Seok Choi

Institutions: Korea Institute of Civil Engineering and Building Technology, Korea University of Science and Technology

Language: English

Topic: Membrane Separation Technologies

Subfield: Water Science and Technology

Field: Environmental Science

Domain: Physical Sciences

SDGs: Responsible consumption and production, Affordable and clean energy

Open Access status: hybrid

Estimated APC paid: $4,580