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Extraction system and extraction method for separating magnesium and extracting lithium from magnesium-containing brine by using secondary amide solvent as well as application of extraction system and extraction method

A technology using secondary amide type and secondary amide type, applied in extraction methods and its application fields, can solve the problems such as failure to complete the large-scale test verification and screening of extractants, and failure to find extraction systems.

Active Publication Date: 2020-01-03
XIANGTAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] However, in general, the extraction method has not yet completed the large-scale test verification and screening of the extractant, and the most suitable extraction system has not been found so far.

Method used

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  • Extraction system and extraction method for separating magnesium and extracting lithium from magnesium-containing brine by using secondary amide solvent as well as application of extraction system and extraction method
  • Extraction system and extraction method for separating magnesium and extracting lithium from magnesium-containing brine by using secondary amide solvent as well as application of extraction system and extraction method
  • Extraction system and extraction method for separating magnesium and extracting lithium from magnesium-containing brine by using secondary amide solvent as well as application of extraction system and extraction method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] Li in the brine of a salt lake in Qaidam Basin, Qinghai + and Mg 2+ The contents are 2.00g / L and 113.43g / L respectively, and the mass ratio of magnesium to lithium is 56.67:1, of which Na + 、K + , Cl - , and B 2 o 3 The contents are 3.83, 1.60, 325.98, 44.00 and 8.14g / L respectively, and the brine density is 1.34g / cm 3 , The brine pH value is 4.3. Take 10mL of this kind of brine in a 100mL ground-mouth Erlenmeyer flask, and then add 30mL of N-octylisobutyramide as an extractant, and the volume ratio of extractant to salt lake brine is 3:1. Put magnets in the Erlenmeyer flask, insert the matching air condenser into the mouth of the flask to prevent the liquid from splashing out, place it in a DF-101S collector type constant temperature heating magnetic stirrer, mix and stir at 20°C, and extract for 30 minutes. Then the mixed liquid was transferred to a 250mL plastic test tube, centrifuged in a LD5-10 desktop centrifuge at a speed of 4500r / min for 15min, the inte...

Embodiment 2

[0054] Take 30mL of N-sec-heptylheptylamide as an extractant in a 100mL ground-necked Erlenmeyer flask, and then add 10mL of the salt lake brine in Example 1, the volume ratio of the extractant to the salt lake brine is 3:1. Put magnets in the Erlenmeyer flask, insert the matching air condenser into the mouth of the flask to prevent the liquid from splashing out, place it in a DF-101S collector type constant temperature heating magnetic stirrer, mix and stir at 20°C, and extract for 30 minutes. Then the mixed liquid was transferred to a 250mL plastic test tube, centrifuged in a LD5-10 desktop centrifuge at a speed of 4500r / min for 15min, the interface between the two phases was clear, and after phase separation, the loaded organic phase after extraction and the remaining brine phase were obtained. Transfer the loaded organic phase to another 100mL ground-mouth Erlenmeyer flask, add deionized water at a volume ratio of 1:6 to the organic phase, and place it in a DF-101S type col...

Embodiment 3

[0060] Take 30mL of N-isooctylheptanamide as the extractant in a 100mL ground-necked Erlenmeyer flask, and then add 10mL of the salt lake brine in Example 1, the volume ratio of the extractant to the salt lake brine is 3:1. Put magnets in the Erlenmeyer flask, insert the matching air condenser into the mouth of the flask to prevent the liquid from splashing out, place it in a DF-101S collector type constant temperature heating magnetic stirrer, mix and stir at 20°C, and extract for 30 minutes. Then the mixed liquid was transferred to a 250mL plastic test tube, centrifuged in a LD5-10 desktop centrifuge at a speed of 4500r / min for 15min, the interface between the two phases was clear, and after phase separation, the loaded organic phase after extraction and the remaining brine phase were obtained. Transfer the loaded organic phase to another 100mL ground-mouth Erlenmeyer flask, add deionized water at a volume ratio of 1:3 to the organic phase, and place it in a DF-101S type coll...

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Abstract

The invention discloses an extraction system and an extraction method for separating magnesium and extracting lithium from magnesium-containing brine by using a secondary amide solvent as well as application of the extraction system and the extraction method. The extraction system contains secondary amide which consists of a single compound or a mixture of two or more compounds, wherein R1 is selected from C2-C12 alkyl or C3-C12 cycloalkyl which comprises a single-ring structure; R2 is selected from C1-C11 alkyl or C3-C11 cycloalkyl which comprises a single-ring structure; the total quantity of carbon atoms in the molecules is 12-18; and the solidifying point of the extraction system is lower than 0 DEG C. According to the extraction method, under a condition that the volume ratio of an organic phase to the brine is (1-10):1, the density of the brine is 1.25-1.38 g / cm<3> and the temperature is 0-50 DEG C, single-stage or multi-stage counter-current extraction and re-extraction are implemented to obtain a low-magnesium-lithium-ratio water phase; and by virtue of concentrated impurity removal and preparation, lithium chloride, lithium carbonate and lithium hydroxide are obtained correspondingly. In the extraction system disclosed by the invention, the molecular structure of the secondary amide is simple; the multi-stage extraction rate of Li<+> is high; the lithium and magnesiumseparation coefficient is large; water is adopted for re-extraction; the consumption of acid and alkaline is greatly reduced; the technological process for extraction and separation is short; the extraction system is small in solution loss; and the extraction system realizes an industrial application value.

Description

technical field [0001] The invention relates to a method for extracting lithium from magnesium-containing brine, in particular to an extraction system, extraction method and application thereof for separating magnesium from magnesium-containing brine to extract lithium by solvent extraction. Background technique [0002] Since this century, the application of lithium in the field of new energy has reached an unprecedented and shocking level in terms of depth and breadth. People have turned thousands of batteries into power sources for electric vehicles, and tens of thousands The combined structure of the metered battery as an energy storage device, the use of lithium materials in 3C products is becoming more and more widespread and popular, and the demand for lithium is increasing day by day. Lithium, as the key positive and negative electrode materials and electrolyte raw materials in batteries, is very important to obtain from natural resources. According to the statistics...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B26/12C22B26/22C22B3/32C01D15/08C01D15/02C01D15/04
CPCC22B26/12C22B26/22C25B1/34C01D15/08C01D15/02C01D15/04C22B3/324C22B3/326C22B3/32Y02P10/20C25B1/46C01D3/06C22B3/26
Inventor 杨立新李聪刘长李志强彭汝军李海博
Owner XIANGTAN UNIV