A method for changing the crystal form of lithium-containing aluminum electrolyte

An aluminum electrolyte and electrolyte technology, applied in the direction of lithium halide, aluminum fluoride, aluminum halide, etc., can solve the problems of insufficient extraction of lithium element, high energy consumption of electrolytic aluminum production, low purity of aluminum electrolyte, etc., and achieve the improvement of current efficiency , low extraction cost, and reduced energy consumption

Active Publication Date: 2019-03-05
NORTHEASTERN UNIV LIAONING
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, since the aluminum electrolyte contains Na 2 LiAlF 6 , NaLi 2 AlF 6 , K 2 LiAlF 6 , KLi 2 AlF 6 and other insoluble lithium salts, these insoluble lithium salts are difficult to dissolve in the acid solution, therefore, the leaching rate of lithium salts is low, and the lithium element in the aluminum electrolyte cannot be fully extracted and recovered, and the purity of the obtained aluminum electrolyte is low, and the production capacity of electrolytic aluminum consumes a lot

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0043] Get 1kg of aluminum electrolyte, obtain aluminum electrolyte powder after crushing and grinding, the content of LiF in the electrolyte is 5%, the content of KF is 1%, the molecular ratio (NaF and AlF 3 The molar ratio) is 2.5:1, select the crushed and finely ground additive sodium sulfate powder, mix the aluminum electrolyte powder and sodium sulfate powder evenly through calculation, and prepare the sum of sodium fluoride, lithium fluoride and aluminum fluoride Molar ratio (LiF+NaF+KF) / AlF 3 It is a mixture of 3.8:1, roasted at 800°C for 4h in a muffle furnace, and the lithium salts in the roasted products obtained are all composed of Na 2 LiAlF 6 , K 2 LiAlF 6 , KLi 2 AlF 6 , NaLi 2 AlF 6 into soluble lithium salts LiF, Li 2 O, L i3 AlF 6 etc., the obtained lithium salt conversion rate was 97.8%.

Embodiment 2

[0045] Get 20kg of aluminum electrolyte, obtain aluminum electrolyte powder after crushing and grinding, the content of LiF in the electrolyte is 5%, the content of KF is 4%, molecular ratio (NaF and AlF 3 The molar ratio) is 2.4:1, and the crushed and finely ground additive potassium carbonate powder is selected, and the aluminum electrolyte powder and potassium carbonate powder are mixed evenly through calculation, and the sum of lithium fluoride, sodium fluoride, and potassium fluoride is prepared and Molar ratio of aluminum fluoride (LiF+NaF+KF) / AlF 3 It is a mixture of 3.5:1, roasted at 500°C for 3h in a belt roaster, and the lithium salt in the roasted product obtained is composed of Na 2 LiAlF 6 , K 2 LiAlF 6 , KLi 2 AlF 6 , NaLi 2 AlF 6 into soluble lithium salts LiF, Li 2 O, L i3 AlF 6 etc., the obtained lithium salt conversion rate was 98.2%.

Embodiment 3

[0047] Get 10kg of aluminum electrolyte, obtain aluminum electrolyte powder after crushing and grinding, the content of LiF in the electrolyte is 7%, the content of KF is 3%, molecular ratio (NaF and AlF 3 The molar ratio) is 2.6:1, select the crushed and finely ground additive sodium oxalate powder, mix the aluminum electrolyte powder and sodium oxalate powder evenly through calculation, and prepare the sum of lithium fluoride, sodium fluoride, and potassium fluoride and Molar ratio of aluminum fluoride (LiF+NaF+KF) / AlF 3 It is a mixture of 3:1, roasted at 300°C for 5h in a belt roaster, and the lithium salts in the roasted products obtained are all composed of Na 2 LiAlF 6 , K 2 LiAlF 6 , KLi 2 AlF 6 , NaLi 2 AlF 6 into soluble lithium salts LiF, Li 2 O, L i3 AlF 6 etc., the obtained lithium salt conversion rate was 95.4%.

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Abstract

The invention discloses a method for changing the crystal form of a lithium-containing aluminum electrolyte, and relates to the technical field of aluminum electrolyte extraction and recovery. It includes the following steps: S1, pulverizing the aluminum electrolyte containing lithium; S2, mixing the additive with the aluminum electrolyte powder, and mixing uniformly to obtain a mixed material, wherein the additive includes an alkali metal oxide other than lithium, and is baked at a high temperature One or more of the alkali metal oxo acid salts other than lithium that can be converted into alkali metal oxides, the alkali metal fluorides and additives contained in the aluminum electrolyte in the mixed material can be converted into The molar ratio of the sum of alkali metal fluorides to aluminum fluoride is greater than 3; S3, roasting the mixed material at high temperature. The invention can convert the insoluble lithium salt in the aluminum electrolyte into a soluble lithium salt, improves the leaching rate of the lithium salt, improves the purity of the aluminum electrolyte, and reduces the energy consumption of electrolytic aluminum production.

Description

technical field [0001] The invention belongs to the technical field of extraction and recovery of aluminum electrolytes, and relates to a method for changing the crystal form of lithium-containing aluminum electrolytes. Background technique [0002] The rapid development of my country's aluminum industry has led to a large consumption of bauxite resources in my country. High-grade bauxite has been scarce, and a large number of low-grade bauxite has been mined and used. This medium and low-grade bauxite contains a large amount of alkali metal elements, especially the bauxite in the main production areas of bauxite in my country has a high content of lithium salt. A large amount of alumina containing lithium salts is used as raw material for electrolytic aluminum production. This alumina is added to the electrolyte, and these lithium salts will be enriched in the aluminum electrolytic cell during use, resulting in an increase in the content of lithium salts in the aluminum el...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C25C3/18
CPCC01D15/02C01D15/04C01F7/54C22B7/00C22B26/12C25C3/18C01P2006/32Y02P10/20
Inventor 王兆文陶文举杨酉坚高炳亮刘风国
Owner NORTHEASTERN UNIV LIAONING
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