Lithium Recovery from Aqueous Resources

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Lithium Recovery from Aqueous Resources ( lithium-recovery-from-aqueous-resources )

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https://doi.org/10.1595/205651317X696676 Johnson Matthey Technol. Rev., 2018, 62, (2) Table V Summary of Reported Studies of Lithium Extraction Using Membrane Processes Mechanism Lithium Separation or separation source Membrane system factor process Ref. Nanofiltration Electrolysis, electrodialysis, dialysis Membrane solvent extraction Grotthuss Sorption Salt lake brine Salt lake brine, seawater Geothermal water, salt lake brine Binary mixtures of Na+, K+ and Mg2+ with Li+* Seawater, geothermal brine Spiral-wound Desal-5 DL 2540C, spiral- wound Desal DK (GE Osmonics, USA); NF90 and XLE (Dow, USA); Spiral-wound DK-1812 (Suntar Membrane Tech, China), DL-2540; 1,4-bis(3-aminopropyl)piperazine (DAPP) and trimesoyl chloride (TMC) polymerised on the polyacrylonitrile (PAN) hollow fibre; ethylenediaminetetraacetic acid (EDTA) functionalised TMC and branched polyethyleneimine (BPEI) Anion exchange MA-7500 (SYBRON); SelemionTM CMV with ionic liquid TMPA-TFSI; Gore-Tex® impregnated with ionic liquid (PP13-TFSI); Li ion conductive glass-ceramics (Ohara Inc, Japan), ACS (Anion exchange) and CIMS (Cation exchange) (ASTOM, Japan) α-acetyl-m-dodecylacetophenone (LIX54) and tri-n-octylphosphine oxide (TOPO) in kerosene embedded in Celgard® 2500 membrane; tributylphosphate (TBP) + FeCl3 in kerosene with polyethersulfone (PES) and sulfonated poly(phthalazinone ether sulfone ketone) (SPPESK) blend; TBP + iron(III) chloride (FeCl3) in kerosene with poly(ethylene-co-vinyl alcohol) (EVAL) PSS threaded HKUST-1 metal-organic framework (MOF) Li1.33Mn1.67O4/PVC, Li1.33Mn1.67O4 encapsulated in polysulfone (PSf)/Kimtex, Li1.33Mn1.67O4/PSf/PAN mixed matrix (nanofibre), LDH‐polyvinylidene fluoride (PVDF)/PVDF hollow fibres + 2+ Li/Mg: 2–42 Highly selective recovery of Li+, Li+/ Mg2+: 12–77 >90% extraction of Li+ in 2 h, high Li+ selectivity Li+/Na+: 35, Li+/Mg2+: 1815 >90% Li+ recovery, complete Li+ selectivity (2, 5, 21, 66–69) (72– 76) (77– 79) (80) (81– 85) the incorporated solvent extraction reagents. Ma et al. (77) reported the first study on the extraction of lithium from geothermal water with the SLM technique. A mixture of extractants consisting of LIX54 (the main component is α-acetyl-m-dodecylacetophenone) and TOPO were immobilised in the Celgard® 2500 membrane having 37–48% porosity. The SLM showed 95% extraction of Li+ in just 2 hours; however, it exhibited stable performance for only up to 72 hours before the flux dropped drastically. The decreased stability was attributed to the pressure difference over the membrane sheet, the solubility of the liquid membrane in the adjacent solutions and emulsion formation of the liquid membrane in aqueous solutions (77). To improve the stability of the SLM for Li+ extraction, a nanoporous ion exchange membrane was fabricated by blending PES with sulfonated poly(phthalazinone ether sulfone ketone) (SPPESK) as a extractant stabiliser (79). With PES/SPPESK blend membrane and TBP and FeCl3 mixed in kerosene as an extractant, Li+ extraction was performed both in a single-stage extraction and a sandwiched membrane extraction contactor system. The best Li+ extraction performance was obtained at a PES:SPPESK ratio of 6:4 and a polymer concentration of 30 wt%. However, these membranes had limited stability in benzene and toluene despite being stable in kerosene (78, 79). To further improve the stability of the membrane with different solvents, EVAL membranes were 169 © 2018 United States Government

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In addition, there are many opportunities to extract Lithium from brine (salt lakes, groundwater, and producer water).

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