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A method for extracting lithium from high aluminum lithium ratio chloride leach solution

A leachate and chloride technology, applied in the chemical industry, can solve problems such as unfavorable industrialization implementation and long-term stable production, and achieve the effects of reducing extraction process costs, low equipment requirements, and reducing corrosion

Active Publication Date: 2021-06-18
江西科丰锂业有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0007] In order to solve the above-mentioned problems in the prior art, the present invention discloses a method for extracting lithium from a high-aluminum-lithium-ratio chloride leaching solution by using a non-saponification extraction method, and abandons the use of neutral phosphorus-oxygen compounds as extraction agents, FeCl 3 The saponification process in the process of extracting lithium as a co-extraction agent avoids the easy precipitation of iron loaded in the organic phase in the saponification process to cause emulsification. Deficiencies in industrialization implementation and long-term stable production

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  • A method for extracting lithium from high aluminum lithium ratio chloride leach solution

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Embodiment 1

[0047] 1) Add the above-mentioned high-aluminum-lithium-ratio chloride leachate and sodium aluminate into the reaction kettle to stir and react. The reaction liquid-solid ratio is 60:1, the reaction temperature is 50°C, the reaction time is 1 hour, and the alkalization degree is controlled at 15 %, the aluminum chloride filtrate was obtained by filtering after the reaction was finished, and was used as the clear solution of the extraction stock solution;

[0048] 2) Use tributyl phosphate as the extractant and 200# kerosene as the diluent, mix tributyl phosphate TBP and 200# kerosene at a volume ratio of 7:3 to obtain a blank organic phase; take one part of the blank organic phase and one part A solution containing 0.1-1mol / L ferric chloride and 0.1-8mol / L hydrochloric acid is mixed, shaken for 10 minutes and then left to separate phases to obtain the extracted organic phase;

[0049] 3) Fully mix 2 parts of the extracted organic phase and 1 part of the extracted raw liquid, a...

Embodiment 2

[0054] 1) Add the above-mentioned high-aluminum-lithium-ratio chloride leaching solution and calcium aluminate into the reaction kettle and stir for reaction. The reaction liquid-solid ratio is 30:1, the reaction temperature is 70°C, the reaction time is 45 minutes, and the alkalization degree is controlled at 8 %, the aluminum chloride filtrate was obtained by filtering after the reaction was finished, and was used as the clear solution of the extraction stock solution;

[0055] 2) Use trioctyl phosphate as the extractant and 200# kerosene as the diluent, mix trioctyl phosphate and 200# kerosene at a volume ratio of 7:3 to obtain a blank organic phase; take one part of the blank organic phase and one part containing Mix a solution of 0.1-1mol / L ferric chloride and 0.1-8mol / L hydrochloric acid, shake for 10 minutes and then stand still for phase separation to obtain the extracted organic phase;

[0056] 3) Fully mix 7 parts of the extracted organic phase and 1 part of the extr...

Embodiment 3

[0060] 1) Add the above-mentioned high-aluminum-lithium-ratio chloride leachate and sodium aluminate into the reaction kettle to stir and react, the reaction liquid-solid ratio is 45:1, the reaction temperature is 45°C, the reaction time is 30 minutes, and the alkalization degree is controlled at 20 %, the aluminum chloride filtrate was obtained by filtering after the reaction was finished, and was used as the clear solution of the extraction stock solution;

[0061] 2) Use tributyl phosphate TBP as the extractant and sulfonated kerosene as the diluent, mix tributyl phosphate TBP and sulfonated kerosene at a volume ratio of 7:3 to obtain a blank organic phase; take a portion of the blank organic phase and a Mix a solution containing 0.1 to 1 mol / L ferric chloride and 0.1 to 8 mol / L hydrochloric acid, shake for 10 minutes and then stand still to separate the phases to obtain the extracted organic phase;

[0062] 3) Fully mix 5 parts of the extracted organic phase and 1 part of ...

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Abstract

The invention provides a method for extracting lithium from a high-aluminum-lithium-ratio chloride leachate, which is suitable for the production process of producing battery-grade lithium chloride and lithium carbonate from the chlorinated leachate of lithium-containing aluminosilicate minerals , the method pre-treats the high-aluminum-lithium ratio chloride leaching solution, so that the aluminum chloride in the leaching solution is hydroxylated to a certain extent, and the extraction stock solution is obtained, and the neutral phosphorus-oxygen compound is prepared as the extraction agent, FeCl 3 It is an extraction system of a co-extractant, forming an extraction organic phase loaded with iron and acid, and the extraction organic phase is fully mixed with the aforementioned extraction stock solution, and a lithium chloride solution is obtained through non-saponification extraction-washing-back extraction. The invention adopts non-saponification extraction to extract lithium with short process flow, good controllability, low cost and low requirements on equipment, and is suitable for industrial application.

Description

technical field [0001] The invention relates to the technical field of chemical industry, in particular to a method for extracting lithium from a chloride leach solution with a high aluminum-lithium ratio. Background technique [0002] Lithium has various excellent properties, and is known as "the energy metal of the 21st century", "industrial monosodium glutamate", "tomorrow's aerospace alloy", and has a significant strategic position. Lithium chloride, together with lithium carbonate and lithium hydroxide, are called the three basic lithium salts. Among lithium deep-processed products, except for battery-grade lithium carbonate and lithium fluoride, which do not need to pass through lithium chloride, other deep-processed products such as lithium metal and butyl Lithium, etc. must pass through the lithium chloride link. Due to the rapid development of lithium batteries and biopharmaceutical industries in recent years, the demand for high-purity metallic lithium and lithium...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B26/12C22B3/38C22B3/44
CPCY02P10/20
Inventor 欧阳红勇李嘉翌
Owner 江西科丰锂业有限公司