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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 IV List of the Adsorptive Properties of H2TiO3 Synthesised Under Different Conditions Synthesis Method Ion sieve Solution Capacity, morphology mg g-1 Ref. Solid state Solid state Solid state using titanium dioxide (TiO2) and LiOH·H2O Sol-gel Low grade Ti, solid state Solid state 700°C Solid state Solid state from LiOH·H2O and TiO2 Sol-gel using CH3COOLi and Ti(OC4H9)4 Uniform particle, 1–2 μm Plate like particles with average diameter of 100–200 nm – Particles size ranges from 20–70 nm 100–300 nm Plate-like particle, 100–300 nm H2TiO3 mixed with poly(vinyl alcohol) (PVA) matrix, porous composite foam Plate-like particle 60–80 nm LiOH (694.1 mg l–1 Li+) Li enriched salt lake brine (1630 mg l–1 Li+, collected from Salar de Uyuni, Bolivia) added with sodium bicarbonate (NaHCO3), pH = 6.5 LiOH (2.0 g l–1 Li+), 25°C LiOH (2.0 g l–1 Li+) LiOH+LiCl Seawater pH = 7.64 LiOH (2.0 g l–1 Li+) LiOH (4.0 g l–1 Li+) 39.8 (45) 32.6 (43) 39.2 (44) Optimum (52) 60°C 57.8 LiOH (4.0 g l–1 Li+), 27.8 (47) 94.5 (46) 30.3 (53) 76.7 (48) Optimum, (49) 27.4 industrial plants due to its various advantages, including low cost, environmental friendliness and easy regeneration. Li/Al LDH materials have a general formula [LiAl2(OH)6]+B-·nH2O, where B = Cl, Br. They are crystallised in hexagonal symmetry with the Li+ located in the vacant octahedral sites within the aluminium hydroxide (Al(OH)3) layer (55). The [LiAl2(OH)6]+ layers are separated by water molecules and hydroxide ions (55). Li/Al LDHs can be synthesised by intercalating the Li+ (in the form of LiCl, LiOH, lithium sulfate (Li2SO4)) into aluminium hydroxides, which are in the form of naturally occurring minerals such as gibbsite (α-Al(OH)3) or bayerite (β-Al(OH)3) (55–59). Recently, alternative synthetic routes such as a solvent-free mechanochemical method have been demonstrated (60, 61). To the best of our knowledge, there exist limited articles in the literature discussing the adsorptive properties of Li/Al LDH. It was first discovered to be a selective sorbent for lithium extraction by Dow Chemical Inc in 1980 (62). The synthesis method was later modified, leading to an increase in the molar fraction of LiX in LiX/Al(OH)3 from 0.2 to 0.33 (63). Commercial granular Li/Al LDH (atomic ratio Li:Al ~0.38) was used in a large scale column system packed with 25 tonnes of sorbent for selective lithium extraction from magnesium- containing brines for more than 200 cycles, demonstrating the good stability of this sorbent (64). Li/Al LDH has a good selectivity for LiCl (the form of Li salts in brine and seawater) compared to other cations, because the distance between Al(OH)3 layers is at the nanoscale such that only ions with small radii can be intercalated (64). Even though the ionic radii of Mg2+ (0.074 nm) and Li+ (0.068 nm) are close, the large polarisability of the Li–Cl bond as compared to the Mg–Cl bond still makes this sorbent Li+ selective (64). Simbol Inc, USA (65) developed a column system packed with Li/Al LDHs for the extraction of lithium salts from geothermal brines sourced from the Salton Sea, California, USA. The geothermal brine has a bulk composition of about 260 ppm Li+, 63,000 ppm Na+, 20,100 ppm K+, 33,000 ppm Ca2+ and other ions (65). The Li/Al LDHs Simbol Inc prepared have a high Li:Al atomic ratio of up to 0.5, which maximises the number of lithium sites available in the layered structure for the intercalation and de-intercalation of lithium from a brine solution 167 © 2018 United States Government

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