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Method for recycling carbon substances in waste cathode leaching residues of aluminum electrolysis cell

A technology for waste and leaching of slag from aluminum electrolytic cells, which is applied in chemical instruments and methods, solid waste removal, transportation and packaging, etc., can solve the problems of low recovery rate, complicated process, neglect of carbon material recovery and resource utilization, etc. To achieve the effect of good adsorption performance, wide source of raw materials, and remarkable adsorption effect

Active Publication Date: 2019-12-03
CENT SOUTH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Most of the above research aims to explore more effective ways of recycling fluoride in the spent cathodes of aluminum electrolytic cells, ignoring the recycling and resource utilization of carbon materials, resulting in serious waste of resources
At present, there are not many industrialized treatments for waste cathode materials of aluminum electrolytic cells. Due to the complex process, high cost, and low recovery rate, they only stay in the laboratory stage, and the resource utilization of waste cathode leaching slag carbon materials is rarely reported.

Method used

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  • Method for recycling carbon substances in waste cathode leaching residues of aluminum electrolysis cell
  • Method for recycling carbon substances in waste cathode leaching residues of aluminum electrolysis cell
  • Method for recycling carbon substances in waste cathode leaching residues of aluminum electrolysis cell

Examples

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Effect test

Embodiment 1

[0062] Take a certain amount of the two-step leaching leaching slag obtained in Comparative Example 1, crush and mix it, and collect spare granules. Among the spare granules, the particles with a particle size of less than 100 mesh account for 90% of the total granule mass. Combine the leaching residue with potassium permanganate in m(KMnO 4 ) / m (leaching slag)=0.25:1g / g mixed, while adding concentrated H with a mass fraction of 98% 2 SO 4 , leached residue and concentrated H 2 SO 4 The liquid-solid ratio is V (concentrated H 2 SO 4 ) / m (leaching slag)=3:1mL / g, stirred at 30°C for 30min, and then stood still for 30min to make the material swellable and then filtered. The expandable material was placed in a muffle furnace at 900°C for 20 seconds to achieve instantaneous expansion, then taken out, and cooled naturally to obtain an expanded graphite-like material. The filtrate was supplemented with appropriate KMnO 4 and concentrated H 2 SO 4 You can continue to use it l...

Embodiment 2

[0067] Take a certain amount of the two-step leaching leaching slag obtained in Comparative Example 1, crush and mix it, and collect spare granules. Among the spare granules, the particles with a particle size of less than 100 mesh account for 80% of the total granule mass. Combine the leaching residue with potassium permanganate in m(KMnO 4 ) / m (leaching slag)=0.55:1g / g mixed, while adding concentrated H with a mass fraction of 75% 2 SO 4 , leached residue and concentrated H 2 SO 4 The liquid-solid ratio is V (concentrated H 2 SO 4 ) / m (leaching slag)=5:1mL / g, stirred at 30°C for 30 minutes, and then stood still for 30 minutes to make the material swellable and then filtered. The expandable material was placed in a muffle furnace at 900°C for 25 seconds to achieve instantaneous expansion, then taken out, and cooled naturally to obtain an expanded graphite-like material. The filtrate was supplemented with appropriate KMnO 4 and concentrated H 2 SO 4 You can continue t...

Embodiment 3

[0072] Take a certain amount of the two-step leaching leaching slag obtained in Comparative Example 1, crush and mix it, and collect spare granules. Among the spare granules, the particles with a particle size of less than 100 mesh account for 100% of the total granule mass. Combine the leaching residue with potassium permanganate in m(KMnO 4 ) / m (leaching slag)=0.85:1g / g mixed, adding mass fraction is 75% concentrated H at the same time 2 SO 4 , leached residue and concentrated H 2 SO 4 The liquid-solid ratio is V (concentrated H 2 SO 4) / m (leaching slag)=3:1mL / g, stirred at 35°C for 40min, and then stood still for 20min to make the material swellable and then filtered. The expandable material was placed in a muffle furnace at 900°C for 20 seconds to achieve instantaneous expansion, then taken out, and cooled naturally to obtain an expanded graphite-like material. The filtrate was supplemented with appropriate KMnO 4 and concentrated H 2 SO 4 You can continue to use ...

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Abstract

The invention relates to a method for recycling the carbon substances in the waste cathode leaching residues of an aluminum electrolysis cell, and belongs to the field of aluminum electrolysis solid waste resource recovery. The method is characterized by uniformly mixing and stirring the aluminum electrolysis cell waste cathode leaching residues subjected to innocent treatment with an oxidant andan intercalator, so that a material becomes expandable and then is filtered, the filter residues are instantaneously expanded at a high temperature and become loose and porous and are repeatedly washed with an aqueous solution after being cooled, the impurities are removed, and then an adsorbing material is prepared and is used for treating the heavy metal wastewater. The filtrate is used circularly after being supplemented with a proper amount of oxidizing agent and the intercalating agent. The specific surface area of the prepared adsorbing material is as high as 26.31 m < 2 > / g, the pore structure is developed, the surface performance is excellent, and the removal rates of a 5mg / L As (III) solution and a 5mg / L Cd (II) solution are 90% or above and 70% or above respectively. The method is short in technological process, the resource utilization of the waste cathode leaching residues of the aluminum electrolysis cell is achieved, the waste is used for treating the waste, the large-scale production is easy, and the better industrial application prospect is achieved.

Description

technical field [0001] The invention relates to a method for recycling carbon materials in the leaching slag of waste cathodes of aluminum electrolytic cells, and belongs to the technical field of comprehensive utilization of solid waste resources of aluminum electrolysis. Background technique [0002] Alumina-cryolite molten salt electrolysis is currently the main method for industrial production of aluminum. Among them, molten cryolite is used as solvent, alumina is used as solute, and carbon body is used as cathode and anode. After a strong direct current is applied, an electrochemical reaction occurs at the two electrodes of the electrolytic cell. Since the cathode carbon block in the electrolytic cell is directly in contact with the high-temperature aluminum liquid and the highly corrosive molten electrolyte (NaF, AlF 3 、Na 3 AlF 6 etc.), the electrolyte melt penetrates into the cathode carbon block, corrodes, deforms inside the cathode carbon block, and locally expa...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B09B3/00
CPCB09B3/80B09B3/40
Inventor 郭朝晖聂云飞肖细元彭驰郭鑫瑶
Owner CENT SOUTH UNIV