A method for efficiently separating fluorine, chlorine, and nitrogen components from aluminum ash to co-produce alumina concentrate

A technology of alumina and aluminum ash, applied in aluminate/alumina/aluminum hydroxide purification, ammonium chloride, alkali metal chloride, etc., to achieve efficient separation and recycling, low investment, and high-efficiency separation

Active Publication Date: 2021-07-09
郑州中科新兴产业技术研究院 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The processing purpose of this technology is mainly to recover the effective components of metal aluminum and aluminum nitride in aluminum ash. Soluble fluoride salts and chloride salts will enter the sodium aluminate solution during the processing process, which may have certain adverse effects on the alumina production system.

Method used

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  • A method for efficiently separating fluorine, chlorine, and nitrogen components from aluminum ash to co-produce alumina concentrate
  • A method for efficiently separating fluorine, chlorine, and nitrogen components from aluminum ash to co-produce alumina concentrate

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Embodiment 1

[0038] In this embodiment, the method for efficiently separating fluorine, chlorine, and nitrogen components from aluminum ash to co-produce alumina concentrate, the specific steps are as follows:

[0039] (1) Desalination and denitrification: Weigh the secondary aluminum ash from an enterprise in Gongyi and put it into the reactor, add water as a solvent according to the ratio of liquid to solid ratio of 2; turn on the stirring and heating control device of the reactor, at 75 Stir at high speed for 2 hours at a temperature of ℃, and the gas generated during the reaction is introduced into the gas absorption device through the pipeline;

[0040] (2) Solid-liquid separation: After the reaction is completed, the slurry is released, and the solid-liquid two-phase is separated by suction filtration;

[0041] (3) Defluorination: Add the separated solid phase and lye with a concentration of 150g / L into the reaction kettle at a ratio of liquid to solid ratio of 2, mix thoroughly, and...

Embodiment 2

[0050] In this embodiment, the method for efficiently separating fluorine, chlorine, and nitrogen components from aluminum ash to co-produce alumina concentrate, the specific steps are as follows:

[0051] (1) Desalination and denitrification: add aluminum ash and water to the reactor according to the ratio of liquid to solid ratio of 1.5, turn on the stirring and heating control device of the reactor, and stir at a high speed for 4 hours at a temperature of 25°C. The gas is introduced into the gas absorption device through the pipeline;

[0052] (2) Solid-liquid separation: After the reaction is completed, the slurry is released, and the solid-liquid two-phase is separated by means of pressure filtration;

[0053] (3) Defluorination: Add the separated solid phase and lye with a concentration of 200g / L into the reaction kettle at a liquid-solid ratio of 1.5, mix well, and react at room temperature of 25°C for 4 hours , the gas produced in the reaction process is introduced in...

Embodiment 3

[0062] In this embodiment, the method for efficiently separating fluorine, chlorine, and nitrogen components from aluminum ash to co-produce alumina concentrate, the specific steps are as follows:

[0063] (1) Desalination and denitrification: Weigh the secondary aluminum ash from an enterprise in Gongyi and put it into the reactor, add water as a solvent according to the ratio of liquid to solid ratio of 2; turn on the stirring and heating control device of the reactor, at 50 Stir at high speed for 3 hours at a temperature of ℃, and the gas generated during the reaction is introduced into the gas absorption device through the pipeline;

[0064] (2) Solid-liquid separation: After the reaction is completed, the slurry is released, and the solid-liquid two-phase is separated by suction filtration;

[0065] (3) Defluorination: Add the separated solid phase and lye with a concentration of 200g / L into the reaction kettle at a liquid-solid ratio of 2, mix well, and then keep warm at...

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Abstract

The invention discloses a method for efficiently separating fluorine, chlorine and nitrogen components from aluminum ash to co-produce alumina concentrate. Aluminum ash and water are added into a reaction kettle for desalination and denitrification treatment, and the slurry after desalination and denitrification treatment is subjected to desalination and denitrification treatment. Solid-liquid separation, after the separated solid phase is fully mixed with lye, the defluorination reaction is carried out. After the defluorination slurry is filtered, washed and separated, a solid-liquid two-phase is obtained, and the obtained solid phase is alumina concentrate; dilute The acid neutralizes the liquid phase to adjust the pH value of the solution to be neutral; the prepared neutral solution and the liquid phase separated after desalination and defluorination are subjected to a solution defluorination reaction; the solution is fully defluorinated. , carry out solid-liquid separation, and the solid phase is fluoride salt; the liquid phase after solid-liquid separation is evaporated and crystallized, and the crystallized product is chloride salt; the present invention obtains ammonia water and chloride salt through desalination, denitrification and defluorination processes. , fluoride salts, high-purity alumina concentrate and other products have realized the efficient separation of alumina, salt and toxic components in aluminum ash.

Description

technical field [0001] The invention relates to the technical field of aluminum ash recycling and utilization produced in electrolytic aluminum and aluminum processing technology, in particular to a method for separating and recovering alumina, chloride salts, fluorine salts and ammonia from aluminum ash. Background technique [0002] Aluminum ash is a solid waste produced during the production of electrolytic aluminum or aluminum processing and smelting. It is mainly composed of cooled metal aluminum, oxides produced during high temperature processes, fluxes, and electrolyte salts. According to literature reports, about 20-40kg of aluminum ash is produced for every 1 ton of primary aluminum produced; about 100-250kg of aluminum ash is produced for every 1 ton of waste aluminum recovered and regenerated. The main components of aluminum ash include alumina, metal aluminum, aluminum nitride, and soluble electrolyte salts; according to different processing links, aluminum ash i...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01F7/46C01F11/22C01D3/04C01C1/16C01B3/02
CPCC01B3/02C01C1/164C01D3/04C01F7/46C01F11/22
Inventor 田登超郭强李永利付明波邵大伟
Owner 郑州中科新兴产业技术研究院
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