Selective Recovery of Lithium from Brines

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Selective Recovery of Lithium from Brines ( selective-recovery-lithium-from-brines )

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Ventura, Bhamidi and Hornbostel The lithium separation coefficients were calculated as follows: Li/Me = QLi/CLi * CMe/QMe where QLi and QMe are the adsorption capacities of Li and a generic metal ion Me in the polymer (mg Li or Me/g sorbent), and while CLi and CMe are the concentrations of Li and metal ion Me in the brine (mg Li or Me/L brine) tested. The concentration of lithium ion and other metal ions were tested by ion exchange chromatography. 3.4 Lithium Adsorption Tests The hybrid sorbent generation was tested for its lithium adsorption and selectivity under variable conditions, including pH, composition and temperature. In a typical experiment, the hybrid nanocomposite fixed bed was tested for its adsorption of Li+ from a synthetic brine containing 255 ppm Li, 10570 ppm Na and 10400 ppm of K in a pH 6 0.4M sodium phosphate buffer solution. The brine was passed through the column at a flow rate of 27 BV/hr (where BV is the bed volume defined as BV= Lr2 with L equal to the length of the sorbent packed bed and r is the radius of the column) and the exiting brine was collected in small fractions. The lithium content of each fraction was measured, and the adsorption experiment was continued until the sorbent was saturated and the exiting brine had the same lithium content as the feed. The sharp breakthrough adsorption curve (Figure 4) indicates that the lithium uptake is fast. Figure4.Breakthrough curve of Li+ from a fixed-column packed with the hybrid nanocomposite sorbent. The brine’s tested composition was: 255 ppm Li, 10570 ppm Na and 10400 ppm of K in a pH 6 0.4M sodium phosphate buffer solution. T= 70oC, flow rate 27 BV/hr. The lithium capacity and selectivity in the presence of high concentrations of Na and K ion are shown in Table 1. It should be noted that, the lithium capacity is calculated from the amount of the lithium released by treatment with 0.5 M HCl, after the sorbent was saturated with Li. Table 1. Sorbent Li capacity and selectivity in synthetic brines at variable pH pH Li brine conc. (mg/L) Na brine conc. (mg/L) K brine conc. (mg/L) Mg brine conc. (mg/L) Ca brine conc. (mg/L) Li capacity (mg Li/g sorbent) Sep. Sep. coeff. coeff Sep. Sep. coeff coeff Li/Mg Li/Ca Li/Na Li/K 7.2 250 17134 10749 - - 16.2 323 107 - - 6 255 10570 10400 - - 14.2 211 77 - - 5 242 10059 - 964 9250 10.8 198 - High * 71 Experimental conditions: flow rate 27BV/hr, temperature 70oC. (*) no Mg uptake was detected. The binding capacity of Mg from synthetic brines containing 964 mg/L of Mg2+ was found to be negligible, with no detected Mg uptake under the experimental conditions summarized in Table 1, therefore, we could not calculate an actual separation coefficient. 4

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