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Stripping method for lithium extraction liquid

An extraction liquid and extraction technology, which is applied in the field of lithium extraction, can solve the problems of potential safety hazards, high equipment costs, and high production costs, and achieve the effects of low maintenance costs, high safety, and low production costs

Active Publication Date: 2021-02-09
ZHEJIANG XINHUA CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, the existing solvent extraction method still has the following problems: (1) strong acid solutions such as hydrochloric acid and sulfuric acid are mainly used for back extraction, and the production cost is high; (2) the strong acid solution used for back extraction makes the acidity too high during back extraction High, the corrosion of equipment on metal materials such as stainless steel is serious, there are potential safety hazards, and the equipment cost is high

Method used

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  • Stripping method for lithium extraction liquid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0059] First take 20mL of benzoyltrifluoroacetone, 20mL of tris(2-ethylhexyl) phosphate, and 60mL of kerosene in a separatory funnel and mix them evenly to obtain the extract, then add alkaline salt lake brine containing 0.26g / L lithium 300mL, no need to adjust the pH value of the brine, shake and extract for 5 minutes, separate the aqueous phase and the loaded extract, extract three times, and combine the loaded extract. Wherein, the pH of the loading extract is 9.

[0060] Mix carbon dioxide and pure water with the above-mentioned loaded extract, and back-extract three times. The single back-extraction time is 5 minutes. The temperature when carbon dioxide is introduced is 25°C, and the pressure is 0.1MPa. It is 1:3. The aqueous phase is collected to obtain the lithium bicarbonate-containing back raffinate, the pH of the back raffinate is 9, and the empty extract is recycled to the extraction stage for further use.

[0061] The aqueous solution of lithium bicarbonate colle...

Embodiment 2

[0064] Take 5mL of benzoyltrifluoroacetone, 5mL of trihexyl phosphate, and 15mL of kerosene in a separating funnel and mix them evenly to obtain the extract, then add 100mL of alkaline salt lake brine containing 2.2g / L lithium, without adjusting the pH of the brine The value was 11, and the aqueous phase and the loaded extract were separated after 10 minutes of shaking extraction, extracted three times, and the loaded extract was combined. Wherein, the pH of the loading extract is 11.

[0065] Mix carbon dioxide and pure water with the above-mentioned loaded extract, and back-extract three times. The single back-extraction time is 5 minutes. The temperature when carbon dioxide is introduced is 20°C, and the pressure is 0.15MPa. It is 1:2. The aqueous phase is collected to obtain the lithium bicarbonate-containing back raffinate, the pH of the back raffinate is 10, and the unloaded extract is recycled to the extraction stage for further use.

[0066] The aqueous solution of l...

Embodiment 3

[0069] First take 75mL of benzoyltrifluorodecanone, 75mL of tripentyl phosphate, and 200mL of kerosene in a separatory funnel and mix them evenly to obtain the extract, then add 700mL of alkaline salt lake brine containing 1.5g / L lithium, without adjustment The pH value of the brine was shaken and extracted for 10 minutes, and the aqueous phase and the loaded extract were separated, extracted three times, and the loaded extract was combined. Wherein, the pH of the loading extract is 10.

[0070] Mix carbon dioxide and pure water with the above-mentioned loaded extract, and back-extract three times. The single-time back-extraction time is 6 minutes. The temperature when carbon dioxide is introduced is 30°C and the pressure is 0.2MPa. 1:1. The aqueous phase is collected to obtain the lithium bicarbonate-containing back raffinate, the pH of the back raffinate is 10, and the unloaded extract is recycled to the extraction stage for further use.

[0071] The aqueous solution of li...

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Abstract

The invention relates to a stripping method for lithium extraction liquid. The stripping method comprises the steps that (1) the lithium extraction liquid is provided, the lithium extraction liquid ismixed with a stripping liquid, and stripping is carried out to obtain stripping raffinate containing lithium bicarbonate, wherein the pH value of the stripping raffinate is 7-11, and the pH value ofthe stripping raffinate is less than or equal to the pH value of the lithium extraction liquid; and (2) the stripping raffinate is heated, and separating is carried out to obtain lithium carbonate. The method can effectively relieve and avoid acidic corrosion of equipment and is high in safety, and the lithium carbonate obtained by the method is high in purity and low in cost.

Description

technical field [0001] The invention relates to the technical field of lithium extraction, in particular to a back-extraction method of lithium extract. Background technique [0002] At present, the solvent extraction method is a very popular new lithium extraction technology at home and abroad, and it uses the special extraction performance of organic solvents to achieve the purpose of lithium extraction. However, the existing solvent extraction method still has the following problems: (1) strong acid solutions such as hydrochloric acid and sulfuric acid are mainly used for back extraction, and the production cost is high; (2) the strong acid solution used for back extraction makes the acidity too high during back extraction High, the corrosion of equipment on metal materials such as stainless steel is serious, there are potential safety hazards, and the equipment cost is high. Contents of the invention [0003] Based on this, it is necessary to address the above problem...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B26/12C22B3/26C01D15/08
CPCC22B26/12C01D15/08C22B3/26Y02P10/20
Inventor 应思斌刘震阿锡他邵卫平吴建仲朱玉成王昶严新华王晓明王俊
Owner ZHEJIANG XINHUA CHEM