A kind of method for preparing high-concentration lithium solution from salt lake brine
A technology of salt lake brine and high-lithium solution, applied in the field of lithium extraction from brine, can solve the problems of harsh extraction process conditions, depletion of lithium-lithium resources, rising production costs, etc., to ensure comprehensive utilization rate, easy to realize automation, and reduce loss rate Effect
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Embodiment 1
[0060] The composition of salt lake brine includes: Li + Concentration 0.08g / L, Na + Concentration 25g / L, Mg 2+ Concentration 5g / L, K + Concentration 0.05g / L, Ca 2+ Concentration 0.003g / L, Cl - Concentration 65g / L, SO 4 2- Concentration 2g / L,CO 3 2- Concentration 0.01g / L, B 3+ Concentration 0.4g / L;
[0061] S1. The control time is 8h, the pressure is lower than 0.3Mpa, and the salt lake brine is adsorbed, replaced and decomposed in sequence. The adsorption flow rate is 3BV, the adsorption temperature is 10℃, and the single-step displacement volume is 0.5 of the total empty volume of the packed resin tower. , the flow rate is 4BV, the temperature is 5°C, and fresh water is used as the raw material; the volume of the first step of analysis is 1.0BV of the empty volume of the packed resin tower, the volume of the second step of analysis is 1.0BV, and the cycle time is 0.2 times the adsorption time, The volume of the third step of analysis is 1.0BV of the empty volume of...
Embodiment 2
[0070] The composition of salt lake brine includes: Li + Concentration 0.13g / L, Na + Concentration 30g / L, Mg 2+ Concentration 11g / L, K + Concentration 1.5g / L, Ca 2+ Concentration 0.2g / L, Cl - Concentration 75g / L, SO 4 2- Concentration 4g / L, CO 3 2- Concentration 1.5g / L, B 3+ Concentration 0.5g / L;
[0071] S1. The control time is 7h, the pressure is lower than 0.3Mpa, and the salt lake brine is adsorbed, replaced and decomposed in sequence. The adsorption flow rate is 2.5BV, the adsorption temperature is 14°C, and the single-step displacement volume is the total empty volume of the filled resin tower. 0.8, the flow rate is 5BV, the temperature is 10°C, and fresh water is used as the raw material; the volume of the first step of analysis is 1.0BV of the empty volume of the filled resin tower, the volume of the second step of analysis is 1.2BV, and the total cycle time of analysis is 1.0BV of the adsorption time. 0.4 times, the volume in the third step of the analysis i...
Embodiment 3
[0080] The composition of salt lake brine includes: Li + Concentration 0.12g / L, Na + Concentration 35g / L, Mg 2+ Concentration 10g / L, K + Concentration 2.5g / L, Ca 2+ Concentration 0.4g / L, Cl - Concentration 85g / L, SO 4 2- Concentration 6g / L, CO 3 2- Concentration 2.0g / L, B 3+ Concentration 0.7g / L;
[0081] S1. The control time is 8h, the pressure is lower than 0.3Mpa, and the salt lake brine is adsorbed, replaced and decomposed in sequence. The adsorption flow rate is 2.5BV, the adsorption temperature is 18°C, and the single-step displacement volume is the total empty volume of the filled resin tower. 1.1, the flow rate is 6BV, the temperature is 15°C, and fresh water is used as the raw material; the volume of the first step of analysis is 1.1BV of the empty volume of the packed resin tower, the volume of the second step of analysis is 1.4BV, and the cycle time is 0.25 times of the adsorption time , the volume of the third step of analysis is 1.1BV of the empty volume...
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