A method for preparing expandable graphite or graphene by utilizing waste cathode carbon formed in electrolytic aluminum production

A technology of expanded graphite and waste cathode, applied in graphene, chemical instruments and methods, production of bulk chemicals, etc., can solve the problems of high energy consumption, high cost, and environmental pollution of electrolytic aluminum waste cathode carbon block

Active Publication Date: 2017-09-26
长沙紫宸科技开发有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, due to the high energy consumption, high cost and secondary pollution of these existing treatment methods, the environmental pollution of the waste cathode carbon blocks of electrolytic aluminum has not been effectively solved, and most of the waste cathode carbon blocks of aluminum electrolytic cells are still discarded.
At pre

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0067] The electrolytic aluminum waste cathode charcoal used in the embodiment of the present invention is taken from the electrolytic cell waste cathode charcoal dismantled in the overhaul of an aluminum plant, and its main chemical components are: C 58.73%, F 9.88%, Na 11.87%, Al 2.44%, Fe 0.75%, Si 4.33%, Ca1.39%, Mg 0.56%, cyanide content 0.22%; The strong oxidizing agent used in the embodiment of the present invention is ZC-HO3 type strong oxidizing agent (by potassium ferrate, potassium dichromate and secondary Potassium chlorate is made in a mass ratio of 2:1:4), purchased from Hunan Xiaoyin Wuji Environmental Energy Technology Development Co., Ltd.; the purity of the hydrazine used in the examples of the present invention is 98.5%.

[0068] (1) Hydrothermal oxidation to produce graphite oxide slurry: crush 10kg of electrolytic aluminum waste cathode carbon to a particle size of less than 6mm, then place it together with 4kg of ZC-HO3 strong oxidant in an oxidation tank ...

Embodiment 2

[0079] The waste cathode charcoal used in the embodiment of the present invention is taken from the bulk electrolytic aluminum waste cathode charcoal stored in the warehouse of an aluminum factory, and its main chemical components are: C 68.03%, F 8.05%, Na 9.21%, Al 2.07% , Fe 0.55%, Si 3.11%, Ca 1.14%, Mg0.57%, cyanide content 0.18%; The strong oxidant used in the embodiment of the present invention is ZC-HO3 type oxidant (by potassium ferrate, potassium dichromate and Potassium hypochlorite is made with a mass ratio of 2:1:4), purchased from Hunan Xiaoyin Wuji Environmental Energy Technology Development Co., Ltd.; the purity of the hydrazine used in the examples of the present invention is 98.5%.

[0080] (1) Hydrothermal oxidation to produce graphite oxide slurry: crush 10kg of electrolytic aluminum waste cathode carbon to a particle size of less than 5mm, then place it in an oxidation tank with a wet grinding mechanism together with 4.8kg of ZC-HO3 strong oxidant, add 90kg...

Embodiment 3

[0091] The electrolytic aluminum waste cathode charcoal used in the embodiment of the present invention is taken from the electrolytic cell waste cathode charcoal dismantled in the overhaul of an aluminum plant, and its main chemical components are: C 58.56%, F 9.86%, Na 11.86%, Al 2.42%, Fe 0.74%, Si 4.33%, Ca1.36%, Mg 0.57%, cyanide content 0.22%; The strong oxidant used in the embodiment of the present invention is ZC-HO3 type oxidant (by potassium ferrate, potassium dichromate and potassium hypochlorite Made at a mass ratio of 2:1:4), purchased from Hunan Xiaoyin Wuji Environmental Energy Technology Development Co., Ltd.; the purity of the hydrazine used in the examples of the present invention is 98.5%.

[0092] (1) Supercritical / liquid carbon dioxide oxidative fluorination conversion: crush 10kg of electrolytic aluminum waste cathode carbon to a particle size below 5mm, then place it in a leaching tank with a rolling and mixing mechanism, use 100kg of liquid carbon dioxid...

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Abstract

A method for preparing expandable graphite or graphene by utilizing waste cathode carbon formed in electrolytic aluminum production is disclosed. The method includes (1) a step of crushing, adding a strong oxidant and water into the crushed product, stirring, rolling or wet-grinding the mixture, and performing a hydrothermal oxidation reaction; (2) a step of controlling the temperature, pressurizing, feeding supercritical or liquid carbon dioxide, mixing the mixture by stirring the mixture, allowing the mixture to stand, adjusting the temperature and pressure, performing separation to obtain aqueous slurry and graphite oxide slurry fluid, and washing the graphite oxide slurry fluid with water to remove impurities; and (3) a step including 1) a manner of performing atomization, expansion and stripping to remove the carbon dioxide; or 2) a manner of adding a reactant for reduction, and then performing atomization, expansion and stripping to remove the carbon dioxide, or further performing denitrification and deoxygenation; or 3) a manner of adding a fluorinating agent, heating the mixture, performing a fluorinating reaction, and performing atomization, expansion and stripping to remove the carbon dioxide. Expanded graphite powder, graphene powder, denitrified deoxygenated graphene powder or fluorinated graphene powder which are prepared by the method have excellent properties. The method is simple, efficient, clean, free of secondary pollution, low in energy consumption and suitable for industrial production.

Description

technical field [0001] The invention relates to a method for preparing expanded graphite or graphene, in particular to a method for preparing expanded graphite or graphene by using electrolytic aluminum waste cathode carbon. Background technique [0002] At present, the output of electrolytic aluminum in my country and the world is developing rapidly. According to statistics, by the end of December 2016, the aluminum smelting enterprises of electrolytic aluminum in my country had built a production capacity of 43.698 million tons, and the operating production capacity had reached 36.739 million tons. With the increase of electrolytic aluminum production, the solid waste produced in the electrolysis process, such as waste cathode carbon, waste anode carbon particles, waste refractory bricks, waste insulation bricks, and waste insulation slag, has also increased rapidly, of which only my country's electrolytic aluminum The annual waste cathode produced by the industry has reac...

Claims

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Application Information

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IPC IPC(8): C01B32/19C01B32/225C01B32/182
CPCC01B2204/04C01B2204/22C01B2204/24C01B2204/32C01P2006/10Y02P20/54
Inventor 尹小林
Owner 长沙紫宸科技开发有限公司
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