Method for extracting lithium from salt lake brine

A salt lake brine and extraction technology, applied in the fields of chemical industry and extraction chemistry, can solve the problems of solvent loss of extractant, strong corrosiveness of extraction equipment, restricting industrial large-scale application, etc., and achieve the effect of improving corrosiveness and simple and reliable operation.

Active Publication Date: 2015-02-18
QINGHAI INST OF SALT LAKES OF CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, this system needs to use high concentration of tributyl phosphate, which is highly corrosive to the extraction equipment, and the extraction agent is not only severely dissolved in water during long-term operation, but also in acidic medium, tributyl phosphate is prone to degradation , especially its severe swelling effect on the materials used to make extraction equipment limits its large-scale industrial application

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] The method for extracting lithium in this salt lake brine provided by the present embodiment includes:

[0018] 1) Prepare the organic phase for extraction: take 500mL of tributyl phosphate and 500mL of N,N-di(2-ethylhexyl)-3-butanoneacetamide to form a composite extractant, take 1000mL of sulfonated kerosene as a diluent and add to the compound in the extractant;

[0019] 2) Extract the water phase: take the salt lake brine of saturated magnesium chloride solution, which is LiCl-MgCl 2 -H 2 O system;

[0020] 3) Add HCl, FeCl to the extracted aqueous phase 3 ·6H 2 O, wherein, the ratio of the amount of substance controlling iron and lithium is 1.3:1, at this moment lithium concentration is 1g / L, and acid concentration is 0.05mol / L;

[0021] 4) Mix the extracted aqueous phase obtained in step 3) with the extracted organic phase obtained in step 1) at a volume ratio of 1:2, fully mix and shake for 6 minutes, then stand still and separate the liquid phases. Detectio...

Embodiment 2

[0023] The method for extracting lithium in this salt lake brine provided by the present embodiment includes:

[0024] 1) Prepare the organic phase for extraction: take 500mL of tributyl phosphate and 500mL of N,N-di(2-ethylhexyl)-3-butanoneacetamide to form a composite extractant, take 1000mL of sulfonated kerosene as a diluent and add to the compound in the extractant;

[0025] 2) Extract the water phase: take the salt lake brine of saturated magnesium chloride solution, which is LiCl-MgCl 2 -H 2 O system;

[0026] 3) Add HCl, FeCl to the extracted aqueous phase 3 ·6H 2 O, wherein, the ratio of the amount of substance controlling iron and lithium is 1.3:1, at this moment lithium concentration is 2g / L, and acid concentration is 0.05mol / L;

[0027] 4) Mix the extracted aqueous phase obtained in step 3) with the extracted organic phase obtained in step 1) at a volume ratio of 1:2, fully mix and shake for 6 minutes, then stand still and separate the liquid phases. Detectio...

Embodiment 3

[0029] The method for extracting lithium in this salt lake brine provided by the present embodiment includes:

[0030] 1) Prepare the organic phase for extraction: take 500mL of tributyl phosphate and 500mL of N,N-di(2-ethylhexyl)-3-butanoneacetamide to form a composite extractant, take 1000mL of sulfonated kerosene as a diluent and add to the compound in the extractant;

[0031] 2) Extract the water phase: take the salt lake brine of saturated magnesium chloride solution, which is LiCl-MgCl 2 -H 2 O system;

[0032] 3) Add HCl, FeCl to the extracted aqueous phase 3 ·6H 2 O, wherein, the ratio of the amount of substance controlling iron and lithium is 1.3:1, at this moment lithium concentration is 3g / L, and acid concentration is 0.05mol / L;

[0033] 4) Mix the extracted aqueous phase obtained in step 3) with the extracted organic phase obtained in step 1) at a volume ratio of 1:2, fully mix and shake for 6 minutes, then stand still and separate the liquid phases. Detectio...

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PUM

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Abstract

The invention provides a method for extracting lithium from salt lake brine. The method comprises the following steps: 1) preparing extract organic phases which comprise a composite extracting agent and a diluent, wherein the composite extracting agent is prepared by mixing tributyl phosphate with N,N-bis(2-ethylhexyl)-3-butanone acetamide according to a volume percent ratio of 50% to 50%; the diluent is sulfonated kerosene; 2) preparing an extract water phase which is an LiCl-MgCl2-H2O system; 3) adding HCl and FeCl3.6H2O to the extract water phase, wherein the ratio of amount of substances of iron and lithium is controlled to be 1.3 to 1, the acid concentration is 0.5mol/L, and the lithium concentration is 1-3g/L; 4) standing after fully mixing the extract water phase obtained in the step 3) with the extract organic phases obtained in the step 1) in a volume ratio of 1 to 2, and then separating a liquid phase. By adopting the method, the problems that the corrosivity of high-concentration tributyl phosphate towards extraction equipment is stronger and the dissolution loss of the extracting agent in water is serious in long-term operation are solved, and the lithium extraction efficiency of the prior art is achieved. The extraction method is simple and reliable to operate.

Description

technical field [0001] The invention belongs to the technical fields of extraction chemistry and chemical industry, and in particular relates to a method for separating lithium from a salt lake brine solution by using a composite extractant. Background technique [0002] my country is rich in salt lake resources, and the salt lake brine is rich in various minerals, which is also an important source of lithium. The reserves of lithium resources in brine in my country rank among the top in the world. However, salt lake brine contains a variety of metal ions, how to separate and extract lithium from it is an important topic of current research. [0003] Lithium not only has important applications in the defense industry, but also has become increasingly important in the national economy, especially in the energy field: 6 Li and 7 Li is an important material for fuel in future nuclear fusion reactors and for nuclear fission reactions, respectively; it is also in increasing dem...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B26/12C22B3/40
CPCY02P10/20
Inventor 姬连敏李丽娟时东李晋峰宋雪雪聂锋宋富根曾忠民
Owner QINGHAI INST OF SALT LAKES OF CHINESE ACAD OF SCI
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