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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

Active Publication Date: 2022-05-24
XIAN LANSHEN NEW MATERIAL TECHNOLOGY CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

From the perspective of practical application, the solar pool heating and lithium sinking method is mainly suitable for carbonate-type brine with high lithium and low magnesium-lithium ratio; the precipitation method is more suitable for brine with medium and low magnesium-lithium ratio; nanofiltration technology in membrane method, Electrodialysis technology is suitable for brine with low magnesium-lithium ratio; calcination method is more suitable for brine with high magnesium-lithium ratio; There are certain restrictions. Lithium-containing raw halogens need to be pretreated by means of concentration and purification. The cycle of the concentration process, the high loss rate of lithium, and the depletion of lithium resources caused by long-term mining will become more and more serious in the future industrial process. The more serious it is, the higher the production cost
In addition, due to environmental pollution caused by organic solvents, harsh extraction process conditions, and high energy consumption, solvent extraction has not been widely used in the production of lithium carbonate from salt lake brine lithium ore.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

The invention discloses a method for preparing a high-concentration lithium solution from salt lake brine. Using salt lake brine as a raw material, the salt lake brine is sequentially adsorbed, replaced and decomposed to obtain lithium solution H1 with high lithium and low salt, and then reverse osmosis membrane technology is used to reverse the lithium solution. Osmotic concentration to obtain lithium-containing brine L2 and low-lithium brine W3; then forced evaporation and concentration of lithium-containing brine L2 to obtain high-lithium solution L3; finally, filtrate refining of high-lithium solution L3, and two-stage filtration to obtain calcium and magnesium ions. For the high-concentration lithium salt solution L5 whose amount is less than 1 ppm, the yield of lithium is 67.9%-87.3%. The present invention has wide applicability, simple process, strong process stability, short production cycle, the utilization rate of lithium resources is more than 70% through the optimized combination in the process, and is environmentally friendly. At the same time, the process can be applied to the extraction of brine with low lithium content Lithium is not affected by the ratio of magnesium to lithium, sodium to lithium, and potassium to lithium in brine, and has very good and extensive industrial application prospects.

Description

technical field [0001] The invention belongs to the technical field of lithium extraction from brine, and in particular relates to a method for preparing high-concentration lithium solution from salt lake brine. Background technique [0002] At present, the main processes for separating lithium from salt lake brine include solar pond heating, precipitation, calcination, membrane, adsorption and solvent extraction. From the perspective of practical application, the solar pond heating lithium precipitation method is mainly suitable for carbonate-type brine with high lithium and low magnesium-lithium ratio; the precipitation method is more suitable for brine with medium and low magnesium-lithium ratio; the nanofiltration technology in membrane method, Electrodialysis technology is suitable for brine with low magnesium-lithium ratio; calcining method is more suitable for brine with high magnesium-lithium ratio; the application of the above technology has an equal effect on the i...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01D15/00C01D15/02C01D15/04C01D15/08
CPCC01D15/00C01D15/02C01D15/04C01D15/08
Inventor 冯志军梅昂冯鹏孙冰杰
Owner XIAN LANSHEN NEW MATERIAL TECHNOLOGY CO LTD
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