US20130115370A1 - Process for preparing inert anode material or inert cathode coating material for aluminium electrolysis - Google Patents

Process for preparing inert anode material or inert cathode coating material for aluminium electrolysis Download PDF

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Publication number
US20130115370A1
US20130115370A1 US13/709,029 US201213709029A US2013115370A1 US 20130115370 A1 US20130115370 A1 US 20130115370A1 US 201213709029 A US201213709029 A US 201213709029A US 2013115370 A1 US2013115370 A1 US 2013115370A1
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United States
Prior art keywords
inert
carbon
aluminium electrolysis
preparing
coating material
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Abandoned
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US13/709,029
Inventor
Xuemin Chen
Jun Yang
Zhihong Li
Weiping WU
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Shenzhen Sunxing Light Alloy Materials Co Ltd
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Shenzhen Sunxing Light Alloy Materials Co Ltd
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Assigned to SHENZHEN SUNXING LIGHT ALLOYS MATERIALS CO., LTD. reassignment SHENZHEN SUNXING LIGHT ALLOYS MATERIALS CO., LTD. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CHEN, XUEMIN, LI, ZHIHONG, WU, WEIPING, YANG, JUN
Publication of US20130115370A1 publication Critical patent/US20130115370A1/en
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B35/00—Boron; Compounds thereof
    • C01B35/02—Boron; Borides
    • C01B35/04—Metal borides
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
    • C25C3/06—Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
    • C25C3/08—Cell construction, e.g. bottoms, walls, cathodes
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
    • C25C3/06—Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
    • C25C3/08—Cell construction, e.g. bottoms, walls, cathodes
    • C25C3/12—Anodes
    • C25C3/125—Anodes based on carbon
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C7/00—Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
    • C25C7/02—Electrodes; Connections thereof

Definitions

  • the disclosure relates to a process for preparing an inert anode material or inert cathode coating material for aluminium electrolysis.
  • aluminium electrolytic industry still employs a conventional Hall-Heroult process; electrolyte always takes cryolite-aluminium oxide as a basic system; an existing pre-baked anode cell mainly adopts a carbon anode and a carbon cathode, where the carbon anode is constantly consumed by oxygen generated to form carbon monoxide and carbon dioxide to be discharged into environment during the electrolytic process, and the carbon cathode can not be wetted by molten aluminium and will suffer long-term corrosion of cryolite.
  • the existing industrial process of titanium boride mainly includes the following three methods:
  • reaction temperature is between 1800 and 1900 DEG C.; if the carbon tube is of vacuum, the reaction temperature can be reduced to between 1650 and 1750 DEG C.; and
  • TiCl 4 +BCl 3 +5H 2 TiB 2 +10HCl; the deposition temperature is between 8000 and 1000 DEG C., at which abrasive and electronic grade products can be made.
  • the titanium boride has good wettability to molten aluminium and can resist the corrosion of cryolite; however, the existing industrial process of titanium boride has disadvantages such as demanding reaction conditions, low reaction yield (less than 90%) and high comprehensive cost of production. Since the titanium boride is expensive, it is difficult to realize the wide application of titanium boride in the process for preparing an inert anode material and an inert cathode material.
  • the inventor has done a great deal of research in the preparation and application of titanium boride and unexpectedly finds that the titanium boride can be prepared without demanding reaction conditions by taking the mixture of fluoborate and fluorotitanate as a raw material, the yield rate of reaction product is high and the reaction product has excellent firmness in preparing an inert anode material or inert cathode coating material for aluminium electrolysis.
  • the disclosure provides a process for preparing an inert anode material or inert cathode coating material for aluminium electrolysis, which includes the following steps:
  • the process provided by the disclosure for preparing the inert anode material or inert cathode coating material for aluminium electrolysis has a simple process and requires no demanding reaction conditions;
  • the intermediate material titanium boride is of a short preparation cycle, has advantages such as high yield rate, big specific surface area, many contact angles and controllable aluminium content, has excellent firmness in preparing the inert anode material or inert cathode coating material for aluminium electrolysis, has good wettability to molten aluminium and high resistance to corrosion of cryolite and can prolong the service life of electrolytic cell; thus, the comprehensive cost of aluminium electrolysis is lower.
  • the fluoborate adopts potassium fluoborate and the fluorotitanate adopts potassium fluotitanate, wherein the reaction formula involved is:
  • the fluoborate adopts sodium fluoborate and the fluorotitanate adopts sodium fluotitanate, wherein the reaction formula involved is:
  • the inert gas is argon gas.
  • the carbon material is one or more of carbon, graphite, asphalt and resin.
  • the disclosure achieves advantages as follows: the process provided by the disclosure for preparing the inert anode material or inert cathode coating material for aluminium electrolysis has a simple process and requires no demanding reaction conditions; the intermediate material titanium boride is of a short preparation cycle, has advantages such as high yield rate, big specific surface area, many contact angles and controllable aluminium content, has excellent firmness in preparing the inert anode material or inert cathode coating material for aluminium electrolysis, has good wettability to molten aluminium and high resistance to corrosion of cryolite and can prolong the service life of electrolytic cell; thus, the comprehensive cost of aluminium electrolysis is lower.

Abstract

The disclosure provides a process for preparing an inert anode material or inert cathode coating material for aluminium electrolysis, which includes the following steps: A) putting aluminium into a reactor, injecting an inert gas to the reactor after vacuumizing, adding the mixture of dried fluoborate and fluorotitanate in the reactor to enable a reaction to form titanium boride and cryolite, and isolating the titanium boride; and B) melting the obtained titanium boride with a carbon material, tamping the melt liquid on a carbon cathode surface, sintering the carbon cathode surface to form the inert cathode coating material for aluminium electrolysis; or, mixing the obtained titanium boride with the carbon material evenly, then high-pressure moulding the mixture, and finally sintering the moulded mixture at a high temperature to form the inert anode material for aluminium electrolysis.

Description

    TECHNICAL FIELD OF THE INVENTION
  • The disclosure relates to a process for preparing an inert anode material or inert cathode coating material for aluminium electrolysis.
    • BACKGROUND OF THE INVENTION
  • At present, aluminium electrolytic industry still employs a conventional Hall-Heroult process; electrolyte always takes cryolite-aluminium oxide as a basic system; an existing pre-baked anode cell mainly adopts a carbon anode and a carbon cathode, where the carbon anode is constantly consumed by oxygen generated to form carbon monoxide and carbon dioxide to be discharged into environment during the electrolytic process, and the carbon cathode can not be wetted by molten aluminium and will suffer long-term corrosion of cryolite. In order to prolong the service life of the electrolytic cell, to reduce the carbon emission to environment and to improve the electrolytic efficiency, it is generally necessary to prepare a cheap inert anode material which can be produced on a large scale or prepare an inert cathode material which can be coated on a carbon cathode surface.
  • The existing industrial process of titanium boride mainly includes the following three methods:
  • (1) direct reaction of titanium and elemental boron at a high temperature: Ti+2B=TiB2;
  • (2) boron carbide process, in which titanium dioxide directly reacts with boron carbide in a carbon tube under the existence of C:
  • 2TiO2+B4C+3C=2TiB2+4CO, if the carbon tube is of H2 atmosphere, the reaction temperature is between 1800 and 1900 DEG C.; if the carbon tube is of vacuum, the reaction temperature can be reduced to between 1650 and 1750 DEG C.; and
  • (3) vapour deposition process, in which TiCl4 and BCl3 are taken as raw materials to perform the following reaction with the participation of H2:
  • TiCl4+BCl3+5H2=TiB2+10HCl; the deposition temperature is between 8000 and 1000 DEG C., at which abrasive and electronic grade products can be made.
  • The titanium boride has good wettability to molten aluminium and can resist the corrosion of cryolite; however, the existing industrial process of titanium boride has disadvantages such as demanding reaction conditions, low reaction yield (less than 90%) and high comprehensive cost of production. Since the titanium boride is expensive, it is difficult to realize the wide application of titanium boride in the process for preparing an inert anode material and an inert cathode material.
    • SUMMARY OF THE INVENTION
  • In order to solve the technical problem existing in the conventional art, the inventor has done a great deal of research in the preparation and application of titanium boride and unexpectedly finds that the titanium boride can be prepared without demanding reaction conditions by taking the mixture of fluoborate and fluorotitanate as a raw material, the yield rate of reaction product is high and the reaction product has excellent firmness in preparing an inert anode material or inert cathode coating material for aluminium electrolysis.
  • The disclosure provides a process for preparing an inert anode material or inert cathode coating material for aluminium electrolysis, which includes the following steps:
  • A) putting aluminium into a reactor, injecting an inert gas to the reactor after vacuumizing, heating the reactor to a temperature of between 700 and 800 DEG C., adding the mixture of dried fluoborate and fluorotitanate in the reactor and stirring quickly to enable a reaction for 4 to 6 hours to form titanium boride and cryolite, then isolating the titanium boride; and
  • B) melting the obtained titanium boride with a carbon material, tamping the melt liquid on a carbon cathode surface, sintering the carbon cathode surface to form the inert cathode coating material for aluminium electrolysis; or, mixing the obtained titanium boride with the carbon material evenly, then high-pressure moulding the mixture, and finally sintering the moulded mixture at a high temperature to form the inert anode material for aluminium electrolysis.
  • With the technical scheme above, the process provided by the disclosure for preparing the inert anode material or inert cathode coating material for aluminium electrolysis has a simple process and requires no demanding reaction conditions; the intermediate material titanium boride is of a short preparation cycle, has advantages such as high yield rate, big specific surface area, many contact angles and controllable aluminium content, has excellent firmness in preparing the inert anode material or inert cathode coating material for aluminium electrolysis, has good wettability to molten aluminium and high resistance to corrosion of cryolite and can prolong the service life of electrolytic cell; thus, the comprehensive cost of aluminium electrolysis is lower.
  • As a further improvement of the disclosure, the fluoborate adopts potassium fluoborate and the fluorotitanate adopts potassium fluotitanate, wherein the reaction formula involved is:

  • K2TiF6+2KBF4+10/3Al=TiB2+10/3[6/5KF.AlF3]
  • As a further improvement of the disclosure, the fluoborate adopts sodium fluoborate and the fluorotitanate adopts sodium fluotitanate, wherein the reaction formula involved is:

  • Na2TiF6+2NaBF410/3Al=TiB2+10/3[6/5NaF.AlF3]
  • As a further improvement of the disclosure, the inert gas is argon gas.
  • As a further improvement of the disclosure, the carbon material is one or more of carbon, graphite, asphalt and resin.
  • Compared with the conventional art, the disclosure achieves advantages as follows: the process provided by the disclosure for preparing the inert anode material or inert cathode coating material for aluminium electrolysis has a simple process and requires no demanding reaction conditions; the intermediate material titanium boride is of a short preparation cycle, has advantages such as high yield rate, big specific surface area, many contact angles and controllable aluminium content, has excellent firmness in preparing the inert anode material or inert cathode coating material for aluminium electrolysis, has good wettability to molten aluminium and high resistance to corrosion of cryolite and can prolong the service life of electrolytic cell; thus, the comprehensive cost of aluminium electrolysis is lower.
    • DETAILED DESCRIPTION OF THE EMBODIMENTS
  • The disclosure is described below in further detail through specific embodiments.
    • Embodiment 1
  • Weighing 2 tons of aluminium and putting it into a reactor, injecting argon to the reactor for protection after vacuumizing, heating the reactor to a temperature of 750 DEG C., adding the mixture of dried potassium fluoborate and potassium fluotitanate in the reactor in accordance with a reaction ratio and stirring quickly to enable a reaction for 5 hours to form titanium boride and cryolite, subjecting the formed titanium boride and cryolite to an existing conventional separation process to obtain titanium boride, drying the titanium boride and weighing it as 1.52 tons, wherein the yield rate of reaction product achieves over 97%.
  • Mixing the obtained titanium boride with resin in accordance with a weight ratio of 90:(1-10), high-pressure sintering the mixture to prepare an inert anode material; mixing the obtained titanium boride with resin in accordance with a weight ratio of 90:(1-10), melting the mixture and tamping the melt liquid on a carbon cathode surface, sintering the carbon cathode surface to form an inert cathode coating material.
    • Embodiment 2
  • Weighing 2 tons of aluminium and putting it into a reactor, injecting argon to the reactor for protection after vacuumizing, heating the reactor to a temperature of 750 DEG C., adding the mixture of dried sodium fluoborate and sodium fluotitanate in the reactor in accordance with a reaction ratio and stirring quickly to enable a reaction for 5 hours to form titanium boride and cryolite, subjecting the formed titanium boride and cryolite to an existing conventional separation process to obtain titanium boride, drying the titanium boride and weighing it as 1.53 tons, wherein the reaction product yield achieves over 97%.
  • Mixing the obtained titanium boride with resin in accordance with a weight ratio of 99:1, high-pressure sintering the mixture to prepare an inert anode material; mixing the obtained titanium boride with resin in accordance with a weight ratio of 99:1, melting the mixture and tamping the melt liquid on a carbon cathode surface, sintering the carbon cathode surface to form an inert cathode coating material.
  • The above are the further detailed description of the disclosure made in conjunction with specific preferred embodiments; it can not be considered that the specific embodiment of the disclosure is only limited to the description above. For the common technicians in the technical field of the disclosure, umpty simple deductions or substitutes can be made without departing from the concept of the disclosure and they are deemed to be included within the scope of protection of the disclosure.

Claims (8)

What is claimed is:
1. A process for preparing an inert anode material or inert cathode coating material for aluminium electrolysis, which includes the following steps:
A) putting aluminium into a reactor, injecting an inert gas to the reactor after vacuumizing, heating the reactor to a temperature of between 700 and 800 DEG C., adding the mixture of dried fluoborate and fluorotitanate in the reactor and stirring quickly to enable a reaction for 4 to 6 hours to form titanium boride and cryolite, then isolating the titanium boride; and
B) melting the obtained titanium boride with a carbon material, tamping the melt liquid on a carbon cathode surface, sintering the carbon cathode surface to form the inert cathode coating material for aluminium electrolysis; or, mixing the obtained titanium boride with the carbon material evenly, then high-pressure moulding the mixture, and finally sintering the moulded mixture at a high temperature to form the inert anode material for aluminium electrolysis.
2. The process for preparing the inert anode material or inert cathode coating material for aluminium electrolysis according to claim 1, wherein the carbon material is one or more of carbon, graphite, asphalt and resin.
3. The process for preparing the inert anode material or inert cathode coating material for aluminium electrolysis according to claim 1, wherein the fluoborate adopts potassium fluoborate and the fluorotitanate adopts potassium fluotitanate.
4. The process for preparing the inert anode material or inert cathode coating material for aluminium electrolysis according to claim 3, wherein the carbon material is one or more of carbon, graphite, asphalt and resin.
5. The process for preparing the inert anode material or inert cathode coating material for aluminium electrolysis according to claim 1, wherein the fluoborate adopts sodium fluoborate and the fluorotitanate adopts sodium fluotitanate.
6. The process for preparing the inert anode material or inert cathode coating material for aluminium electrolysis according to claim 5, wherein the carbon material is one or more of carbon, graphite, asphalt and resin.
7. The process for preparing the inert anode material or inert cathode coating material for aluminium electrolysis according to claim 1, wherein the inert gas is argon gas.
8. The process for preparing the inert anode material or inert cathode coating material for aluminium electrolysis according to claim 7, wherein the carbon material is one or more of carbon, graphite, asphalt and resin.
US13/709,029 2012-05-23 2012-12-09 Process for preparing inert anode material or inert cathode coating material for aluminium electrolysis Abandoned US20130115370A1 (en)

Applications Claiming Priority (2)

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CN201210161985.7A CN102660757B (en) 2012-05-23 2012-05-23 Preparation technology for inert anode material or inert cathode coating material for aluminum electrolysis
CN201210161985.7 2012-05-23

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EP (1) EP2666887B1 (en)
CN (1) CN102660757B (en)
ES (1) ES2534969T3 (en)
WO (1) WO2013174067A1 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111534837B (en) * 2020-05-07 2021-07-09 北京科技大学 Preparation method of inert anode suitable for high-temperature molten salt system

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Publication number Publication date
ES2534969T3 (en) 2015-04-30
EP2666887B1 (en) 2015-02-18
EP2666887A1 (en) 2013-11-27
CN102660757A (en) 2012-09-12
CN102660757B (en) 2015-01-21
WO2013174067A1 (en) 2013-11-28

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