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Extraction of Lithium from Brine Chemistry

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Extraction of Lithium from Brine Chemistry ( extraction-lithium-from-brine-chemistry )

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While established, the chemistry outlined above also has these drawbacks: • Solar evaporation loses most of the water in the brine to the atmosphere, thus the aquifer is depleted of its water. While it could be argued that this does not matter because the water will return as rain, that rain is unlikely to occur at the salar concerned, because salars are by nature found in arid regions. • Solar evaporation of the brine generates large amounts of chloride salt that must be disposed of on large dumps, precluding other uses for the land area concerned. Again, this may not matter because the salar is in a sparsely populated, arid region. Even so, increasingly stringent environmental constraints could mitigate against new projects using the established chemistry to extract lithium from salar brines. Chemistry using lithium-selective solvent extraction An approach that does not require solar evaporation, and therefore will not deplete the aquifer of water or generate large dumps of salt, is enabled by solvent extraction technology that very selectively extracts lithium away from other monovalent cations. The Clayton Valley Lithium Project [10] uses this solvent extraction to very selectively extract lithium from a feed brine of the composition shown in Table 4. A facet of the solvent extraction system used is that it is only selective for lithium against other monovalent cations, and higher-valent cations are extracted ahead of lithium. Therefore, higher-valent cations (Ca2+, Mg2+, etc.) need to be fully removed from the brine ahead of the solvent extraction step. The Clayton Valley Lithium Project uses membrane technology, the membrane selected for its ability to allow monovalent cations to pass while blocking the passage of higher-valent ions. The composition of the permeate obtained is shown in Table 4. Table 4 – Clayton Valley feed brine and permeate, mg/L Brine Mg Ca Na K Li SO4 B Feed brine 409 796 38400 3850 209 4740 26 Permeate <3 <3 35900 3670 210 <3 21 Lee et al. [11] give the following stoichiometry for the selective solvent extraction of lithium, the bold print denoting the organic phase: xLi+ + xOH− +nHDBM + mTOPO → xLiDBM + (n-x)HDBM•mTOPO + xH2O xLiDBM + (n-x)HDBM•mTOPO + xH3O+ → xLi+ + nHDBM + mTOPO + xH2O TOPO means trioctylphosphine oxide and HDBM means dibenzoylmethane (1,3-diphenyl-1,3- propanedione). The above stoichiometry could equally well have been written without the OH− ion on the left and with a proton on the right instead of water. The proton released by the extraction has to be neutralised, and sodium hydroxide is the most convenient base. That means that the selective solvent extraction of lithium replaces each Li+ cation extracted with one Na+ cation. The membrane separation ahead of the solvent extraction stage removes the need for other reagents ahead of solvent extraction. Anions are not extracted, therefore there is no need to remove boron or sulphate from the feed to the solvent extraction step, although the membrane step ahead of that does reject sulphate. Presented at the Critical Materials Symposium, EXTRACTION 2018, Ottawa, August 26-29

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