Method for separating lithium from salt lake raw bittern
A brine and raw halogen technology, applied in the field of development and application of new energy raw materials for lithium batteries, can solve the problems of low lithium yield, difficult potassium impurities, and high production and processing costs, reducing lithium loss, simple and easy operation, and improving utilization rate. Effect
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Embodiment 1
[0042] The salt lake brine is composed of lithium ion concentration 0.26g / L, boron ion concentration 0.3g / L, potassium ion concentration 11g / L, magnesium ion concentration 24g / L, sodium ion concentration 69g / L, chloride ion concentration 165g / L, sulfate radical The ion concentration is 7.5g / L.
[0043] S1. The time to realize the steps of the whole control process is 7 hours.
[0044] S2, using the above-mentioned brine as raw material, the feed flow rate is controlled at 0.5BV / h, and adsorption is carried out, and the concentration of lithium ions in the discharged tail liquid is measured to be 0.053g / L, and the recovery rate of lithium is 79.6%;
[0045] S3. Switch the adsorption column saturated with S2 to the top liquid area, and use the RO product water with a temperature of 20°C and a feed flow rate of 1.0BV / h as the top liquid medium to carry out top liquid;
[0046] S4. Switch the adsorption column saturated with adsorption of S3 to the desorption zone, and perform an...
Embodiment 2
[0049] The composition of salt lake brine is lithium ion concentration 0.35g / L, boron ion concentration 0.35g / L, potassium ion concentration 11.5g / L, magnesium ion concentration 26g / L, sodium ion concentration 75g / L, chloride ion concentration 175g / L, sulfuric acid The root ion concentration is 9g / L.
[0050] S1. The time to realize the steps of the whole control process is 8 hours.
[0051] S2, using the above-mentioned brine as raw material, the feed flow rate is controlled at 0.5BV / h, and adsorption is carried out, and the concentration of lithium ions in the discharged tail liquid is measured to be 0.063g / L, and the recovery rate of lithium is 82%;
[0052] S3. Switch the adsorption column saturated with adsorption of S2 to the top liquid zone, and use the RO product water with a temperature of 21°C and a feed flow rate of 1BV / h as the top liquid medium to carry out top liquid;
[0053] S4. Switch the adsorption column saturated with adsorption of S3 to the desorption zon...
Embodiment 3
[0056] The salt lake brine is composed of lithium ion concentration 0.26g / L, boron ion concentration 0.3g / L, potassium ion concentration 11g / L, magnesium ion concentration 24g / L, sodium ion concentration 69g / L, chloride ion concentration 165g / L, sulfate radical The ion concentration is 7.5g / L.
[0057] S1. The time to realize the steps of the whole control process is 8 hours.
[0058] S2, using the above-mentioned brine as a raw material, the feed flow rate is controlled at 1.5BV / h, and adsorption is carried out. The lithium ion concentration in the tail liquid is measured to be 0.065g / L, and the lithium yield is 75%;
[0059] S3. Switch the adsorption column saturated with adsorption of S2 to the top liquid zone, and use the RO product water with a temperature of 22°C and a feed flow rate of 1.4BV / h as the top liquid medium to carry out top liquid;
[0060] S4. Switch the adsorption column saturated with adsorption of S3 to the desorption zone, and perform analysis with RO p...
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