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Ion rectification method for preparing lithium chloride from salt lake brine

A technology of salt lake brine and lithium chloride, which is applied in the field of ion distillation for the production of lithium chloride, can solve problems such as limiting the separation efficiency of target ions, unsatisfactory screening performance, and continuous operation characteristics that cannot be effectively reflected. Reduce the requirements for its own characteristics, simplify the construction method, and improve the effect of purity and quality

Active Publication Date: 2021-11-19
UNIV OF SCI & TECH OF CHINA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Therefore, in the selective electrodialysis process, the separation performance of special ions still depends on the screening characteristics of the functional membrane itself, and the unsatisfactory screening performance of the functional membrane also limits the separation efficiency of target ions.
[0006] Similar to the traditional special ion separation process, such as ion exchange, solvent extraction, ion sieve adsorption, etc., the industry needs to achieve the target screening of lithium ions through the coupling and integration of multiple selective electrodialysis units. At this time, selective electrodialysis itself The characteristics of continuous operation cannot be effectively reflected

Method used

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  • Ion rectification method for preparing lithium chloride from salt lake brine
  • Ion rectification method for preparing lithium chloride from salt lake brine
  • Ion rectification method for preparing lithium chloride from salt lake brine

Examples

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Embodiment 1

[0057] The present embodiment utilizes the above-mentioned ion rectification system to process the simulated high magnesium-lithium ratio salt lake brine, the main components of the simulated brine are lithium ions, magnesium ions, and chloride ions, and the adopted ion rectification system is a four-stage ion rectification system, The number of ion rectification units is 1; the first-stage anion rectification chamber is communicated with the first-stage cation rectification chamber, and the circulating flow is driven by a solution-driven pump; the second-stage anion rectification chamber is communicated with the second-stage cation rectification chamber, The circulation flow is driven by the solution-driven pump; the third-stage anion rectification chamber is communicated with the third-stage cation rectification chamber, and the circulation flow is driven by the solution-driven pump; the fourth-stage anion rectification chamber is communicated with the fourth-stage cation rect...

Embodiment 2

[0061] The present embodiment utilizes the above-mentioned ion rectification system to process the simulated salt lake brine. The main components of the simulated brine are lithium ions, magnesium ions, chloride ions, and sulfate ions. The ion rectification system used is a four-stage ion rectification system. The number of distillation units is 1. The first-stage anion rectification chamber is communicated with the first-stage cation rectification chamber, and the circulating flow is driven by the solution-driven pump; the second-stage anion rectification chamber is communicated with the second-stage cation rectification chamber, and the circulation flow is driven by the solution-driven pump; The third-stage anion rectification chamber is communicated with the third-stage cation rectification chamber, and the circulating flow is driven by the solution-driven pump; the fourth-stage anion rectification chamber is communicated with the fourth-stage cation rectification chamber, a...

Embodiment 3

[0065] In this embodiment, the above-mentioned ion distillation system is used to process the actual salt lake old brine. The main components of the salt lake brine are lithium ion, magnesium ion, calcium ion, chloride ion and sulfate ion, and the adopted ion rectification system is four-stage ion rectification. system, the number of ion distillation units is 1. The first-stage anion rectification chamber is communicated with the first-stage cation rectification chamber, and the circulating flow is driven by the solution-driven pump; the second-stage anion rectification chamber is communicated with the second-stage cation rectification chamber, and the circulation flow is driven by the solution-driven pump; The third-stage anion rectification chamber is communicated with the third-stage cation rectification chamber, and the circulating flow is driven by the solution-driven pump; the fourth-stage anion rectification chamber is communicated with the fourth-stage cation rectificat...

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Abstract

The invention discloses an ion rectification method for preparing lithium chloride from salt lake brine. According to the method,an ion rectification system is adopted, and the ion rectification system is formed by sequentially laminating a plurality of monovalent and multivalent cation selective membranes and a plurality of monovalent and multivalent anion selective membranes according to the principle that the same kind of membranes is arranged at the same side, and then adding a flow channel separation net and a sealing gasket; chloride ions and lithium ions are selectively screened by the plurality of multivalent anion selective membranes and the multivalent cation selective membranes respectively, impurity anions and cations are selectively blocked at the same time; and finally, through n-stage selective separation, the stage number of the selectivity coefficient among the chloride ions, the lithium ions and the impurity ions is amplified, and therefore, efficient extraction of the lithium chloride is realized in a single electrodialysis membrane assembly. According to the method of the invention, the selectivity coefficient of the lithium ions and the chloride ions is determined by the number of the monovalent and multivalent cation selective membranes and the monovalent and multivalent anion selective membranes which are used in a laminated manner, so that the requirement on the characteristics of a special diaphragm is greatly reduced, and the purity and the quality of a salt lake lithium extraction product are greatly improved.

Description

technical field [0001] The invention belongs to the field of electrically driven membrane separation, in particular to an ion distillation method for preparing lithium chloride from salt lake brine. Background technique [0002] Special ion separation is an important chemical separation technology, which occupies an important position in the field of lithium extraction from salt lakes. Lithium is the lightest metal with extremely strong electrochemical activity. Its metals and compounds have been rapidly developed in the fields of high-energy lithium batteries, nuclear fusion power generation, aerospace, ceramics, lasers, and medicine. From the perspective of economic development and national security, many countries have taken it as a strategic material reserve and carried out applied technology research, and all countries in the world have also attached great importance to the development of lithium resources. The reserves of lithium resources in my country ranks second i...

Claims

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Application Information

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IPC IPC(8): C01D15/04B01D61/48B01D61/58B01D61/14C02F1/44C02F1/469
CPCC01D15/04B01D61/48B01D61/58B01D61/145B01D61/147C02F1/444C02F1/4693C01P2006/80Y02P10/20
Inventor 徐铜文陈秉伦蒋晨啸
Owner UNIV OF SCI & TECH OF CHINA
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