EP1567692B1 - Procede de conditionnement d'anodes a base d'alliage de fer pour des cellules d'extraction electrolytique d'aluminium - Google Patents

Procede de conditionnement d'anodes a base d'alliage de fer pour des cellules d'extraction electrolytique d'aluminium Download PDF

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EP1567692B1
EP1567692B1 EP03775701A EP03775701A EP1567692B1 EP 1567692 B1 EP1567692 B1 EP 1567692B1 EP 03775701 A EP03775701 A EP 03775701A EP 03775701 A EP03775701 A EP 03775701A EP 1567692 B1 EP1567692 B1 EP 1567692B1
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metallic
anode structure
iron
anode
aluminium
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EP1567692A1 (fr
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Jean-Jacques Duruz
Vittorio De Nora
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Moltech Invent SA
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Moltech Invent SA
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    • 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
    • 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

Definitions

  • This invention relates to the conditioning of iron alloy based aluminium electrowinning anodes to form an integral electrochemically active iron-based oxide layer thereon, anodes so conditioned, aluminium electrowinning cells with such anodes and the production of aluminium in such cells.
  • EP Patent application 0 306 100 (Nyguen/Lazouni/Doan )
  • US Patents 5,069,771 , 4,960,494 and 4,956,068 (all Nyguen/Lazouni/Doan ) describe metallic anode substrates which may be further covered with such an in-situ formed protective cerium oxyfluoride layer.
  • US Patent 5,510,008 discloses an anode made from an inhomogeneous porous metallic body obtained by micropyretically reacting a powder mixture of nickel, iron, aluminium and possibly copper and other elements.
  • An electrochemically active oxide-based outer portion is formed by in-situ polarisation.
  • WO00/06803 (Duruz/de Nora/Crottaz ), WO00/06804 (Crottaz/Duruz ) and WO01/42534 (de Nora/Duruz ) disclose anodes produced from nickel-iron alloys which are surface oxidised to form a coherent and adherent outer iron oxide-based layer whose surface is electrochemically active surface.
  • WO01/42534 discloses a nickel-iron alloy aluminium electrowinning anode with an openly porous electrochemically active surface produced by removal of iron from the surface, in particular by electrolytic dissolution of iron.
  • WO00/06805 discloses an aluminium electrowinning anode having a metallic anode body which can be made of various alloys, for example a nickel-iron-copper alloy.
  • the surface of the anode body is oxidised by anodically evolved oxygen to form an integral electrochemically active oxide-based surface layer.
  • the oxidation rate of the anode body is equal to the rate of dissolution of the surface layer into the electrolyte. This oxidation rate is controlled by the thickness and permeability of the surface layer which limits the diffusion of anodically evolved oxygen to the anode body.
  • WO01/42536 discloses an aluminium electrowinning anode made form a nickel-iron alloy having an openly porous outer portion which consists predominantly of nickel metal and which is obtainable by removal of iron from the alloy.
  • WO01/42534 disclose further metal-based aluminium electrowinning anodes.
  • Metal or metal-based anodes are highly desirable in aluminium electrowinning cells instead of carbon-based anodes.
  • the anodes are pre-oxidised in an oxidising atmosphere before use to produce an electrochemically active oxide layer thereon.
  • the metal-based anodes are usually pre-heated above the molten electrolyte to inhibit thermal shocks in the electrolyte and its solidification when the anode is immersed.
  • a major object of the invention is to provide a method of conditioning an iron-based alloy anode for aluminium electrowinning to increase its lifetime and improve its electrical conductivity during use.
  • Another object of the invention is to provide a method of conditioning an iron-based alloy anode to form an active anode surface that has a high electrochemical activity for the oxidation of oxygen ions for the formation of bimolecular gaseous oxygen and a low solubility in the electrolyte.
  • a further object of the invention is to provide a method of conditioning an iron-based alloy anode to form an integral electrochemically active oxide layer with an improved density and coherence and with limited ionic conductivity for oxygen ions and a low electrical resistance.
  • Yet another object of the invention is to provide a method of conditioning an aluminium electrowinning anode which is made of readily available alloys(s).
  • Yet a further object of the invention is to provide an aluminium electrowinning anode which is made of readily available alloys(s) and an aluminium electrowinning cell having such an anode.
  • the invention is based on the observation that an integral oxide layer formed by oxidation of an iron-based alloy, in particular an iron-based alloy comprising nickel and/or cobalt, is significantly denser and more coherent when the oxidation of the iron-based alloy is carried out by polarisation thereof in a molten electrolyte under specific conditions compared to oxide layers produced by conventional oxidation in air or by polarisation in a molten electrolyte as disclosed in the prior art.
  • the anode's active surface is up to immersion into the electrolyte essentially metallic and substantially unreacted with reactive species that form ceramic compounds with metals from the iron-based alloy.
  • reactive species include oxygen at or above ambient temperature or fluorine-containing gases that could contact the anode while pre-heating the anode above the cell.
  • the invention relates to a method of conditioning a metallic anode structure for producing aluminium in a molten electrolyte containing dissolved alumina.
  • the metallic anode structure has initially an iron-based alloy outer part with an active anode surface which is essentially metallic and free of any ceramic compounds, in particular oxides and fluorides, of metals from the metallic anode structure.
  • the method comprises the ordered steps of: (a) substantially preventing the essentially metallic active surface free of said ceramic compound from reacting with any reactable species, in particular oxygen and fluorine species, until immersion into a molten electrolyte containing oxygen ions; (b) immersing into the molten electrolyte the metallic anode structure with its essentially metallic active surface free of said ceramic compounds; and (c) polarising the immersed metallic anode structure at a potential above the potential of oxidation of oxygen thereby evolving oxygen on the active anode surface and oxidising the active anode surface to form on the metallic anode structure a dense and coherent integral iron-based oxide layer which is electrochemically active for the oxidation of oxygen and which inhibits diffusion of oxygen towards the metallic anode structure.
  • the prevention of the metallic active surface from reacting with any reactable species, in particular oxygen and fluorine species, until immersion into a molten electrolyte can be achieved either by protecting the active surface against reaction, for instance by coating the surface with a temporary protective layer, or by avoiding exposure of the active surface to a reactive environment for an extended period of time during which a significant amount of anode constituents at the active surface can react with the environment.
  • the method of conditioning the iron-based alloy anodes of the present invention prevents substantially any reactive interactions between the anode and the environment before immersion into the molten electrolyte.
  • the anode's alloy contains at its surface a noticeable amount of ceramic compounds produced by reaction of metals from the alloy's surface with a reactive environment, such ceramic compounds should be removed from the alloy's surface before carrying out the method of the invention.
  • the method of the invention includes the step of pre-heating the metallic anode structure, prior to its immersion, to a temperature at which it can be immersed into the molten electrolyte without substantial solidification thereof.
  • the structure's essentially metallic active surface is maintained free of said ceramic compounds by substantially preventing the active anode surface from reacting with the environment during pre-heating before immersion. This is not the case with prior art methods, when the anodes are pre-heated without the inventive conditioning.
  • Protection of the active anode surface prior to immersion into the molten electrolyte can be achieved by covering the active surface with a temporary protective layer which is substantially impermeable to any species reactable with the active surface and which is removed prior to immersion into the molten electrolyte or dissolves therein as a fugitive coating.
  • the temporary layer should be heat stable, for instance applied from a ceramic paint, e.g. an alumina-based paint, which is stable also at high temperature.
  • a heat-stable protective coating can be used even if the anode is not subjected to a preheat treatment.
  • the temporary layer for longlasting protection at ambient temperature before use can be an organic paint or a substantially impervious wrapping, e.g. made of plastic.
  • the anode structure can also be pre-heated prior to immersion in an inert atmosphere that is substantially free from any species reactable with the active surface. In this case, no heat stable temporary protective layer is needed during the pre-heating.
  • the iron-based alloy outer part may comprise one or more elements selected from nickel, cobalt, copper, molybdenum, manganese, titanium, tantalum, tungsten, hafnium, vanadium, zirconium, niobium, chromium, cobalt, aluminium, silicon, carbon and the rare earth metals, in particular yttrium.
  • the iron-based alloy outer part consists essentially of: 45-55 weight% iron; 15-55 weight% in total of nickel and/or cobalt; 0-30 weight% copper; and 0-10 weight% in total of one or more further elements, usually selected from molybdenum, manganese, titanium, tantalum, tungsten, hafnium, vanadium, zirconium, niobium, chromium, cobalt, aluminium, silicon, carbon and the rare earth metals, in particular yttrium.
  • the metallic anode structure can be a cast alloy. Casting can be advantageously used to produce anodes of complex shapes, e.g. specially adapted for the circulation of electrolyte. Examples of such anode shapes are disclosed in WO99/02764 (de Nora/Duruz ), WO00/40781 , WO00/40782 and WO03/006716 (all de Nora ).
  • the metallic anode structure can be quenched and/or annealed prior to immersion into the molten electrolyte, taking care however that the anode's active surface is not exposed to an environment that can substantially react with anode constituents at the active surface.
  • the invention also relates to a method of conditioning or reconditioning a metallic anode structure for producing aluminium in a molten electrolyte containing dissolved alumina, for example when the metallic anode structure has been impaired by exposure to a reactive environment before use or when the anode structure has been worn during use.
  • Such a used or impaired metallic anode structure comprises an iron-based alloy outer part having a surface which is covered with ceramic compounds, in particular oxides and fluorides, of metals from the outer part.
  • the conditioning or reconditioning method comprises the steps of: removing substantially all ceramic compounds from the surface of the outer part to form an essentially metallic active anode surface; and then conditioning as described above the metallic anode structure with its essentially metallic active anode surface free of any ceramic compounds.
  • a further aspect of the invention relates to method of electrowinning aluminium.
  • This method comprises the steps of: conditioning a metallic anode structure as described above including polarising it in a molten electrolyte to form on the anode structure a dense and coherent integral iron-based oxide layer; and electrolysing dissolved alumina in the same or a different molten electrolyte using the conditioned anode structure to evolve oxygen thereon and produce aluminium on a facing cathode.
  • the dense and coherent integral iron-based oxide layer of the anode structure can be further formed during electrolysis by slow oxidation of the metallic anode structure at the metallic structure/oxide layer interface.
  • Constituents of the dense and coherent integral iron-based oxide layer at the oxide layer/electrolyte interface may slowly dissolve into the electrolyte during electrolysis, preferably at a rate corresponding to the oxidation rate of the metallic anode structure at the metallic structure/oxide layer interface, as disclosed in WO00/06805 (de Nora/Duruz ).
  • the aluminium production molten electrolyte can comprise an amount of dissolved iron species and dissolved alumina sufficient to inhibit significantly dissolution of constituents of the dense and coherent integral iron-based oxide layer at the oxide layer/electrolyte interface.
  • the anode can be protected against the electrolyte with a cerium oxyfluoride-based outermost coating deposited and/or maintained during use, for example as disclosed in the abovementioned US Patents 4,614,569 , 4,680,094 , 4,683,037 and 4,966,674 .
  • the aluminium production molten electrolyte is maintained at a temperature below 960°C, preferably between 840°C and 940°C.
  • the aluminium production molten electrolyte can contain NaF and AlF 3 in a molar ratio in the range from 1.2 to 2.4.
  • the alumina content in the aluminium production molten electrolyte is usually below 10 weight%, typically between 5 weight% and 8 weight%.
  • alumina-depleted electrolyte is circulated away from the electrochemically active iron-based oxide layer, enriched with alumina, and alumina-enriched electrolyte is circulated towards the electrochemically active iron-based oxide layer.
  • Such an electrolyte circulation can be achieved by following the teachings of WO99/41429 (de Nora/Duruz ), WO99/41430 (Duruz/Bell ⁇ ), WO00/40781 , WO00/40782 , WO01/31088 and WO03/006716 (all de Nora ).
  • Another aspect of the invention relates to an aluminium electrowinning anode structure.
  • This structure comprises an iron-based alloy metallic outer part covered with a dense and coherent integral iron-based oxide layer obtainable by conditioning by the above described method a metallic anode structure having an iron-based alloy outer part with an active anode surface which is essentially metallic and free of any ceramic compounds of metals from the metallic anode structure.
  • the anode of the invention Compared to pre-oxidised anodes or anodes that are pre-heated unprotected in fumes above the molten electrolyte, the anode of the invention exhibits upon use in an aluminium electrowinning cell a more protective denser and more coherent oxide layer which is thinner and more conductive, as demonstrated in the example.
  • the invention also relates to an aluminium electrowinning anode structure having an iron-based alloy metallic outer part with an active anode surface.
  • the active surface is essentially metallic and free of any ceramic compounds of metals from the metallic anode structure and is covered with a temporary protection medium.
  • This protective medium substantially prevents ceramic-forming reactions at the essentially metallic anode surface and is separable from the active surface prior to immersion into the molten electrolyte or by contact with the molten electrolyte.
  • the temporary protection medium is removable prior to immersion into the electrolyte or soluble in the electrolyte.
  • the temporary protection medium may comprises one or more substantially impervious solid layers. Suitable layers comprise at least one of ceramics, such as alumina, including ceramics applied from colloids, for instance colloidal alumina precursor, such as Nyacol TM and/or Condea TM , and other colloid precursors of ceramics; metals, in particular reactable metals, such as aluminium, iron, copper, chromium or yttrium, for reacting with possibly diffusing reactive gases; polymers, e.g. plastic, in particular wrapping the anode structure under vacuum or inert gas or carrying one or more of the above layer constituents.
  • the temporary protection medium can comprise an inert liquid or viscous material, such as oil or grease, or an inert gas, such as nitrogen or carbon dioxide, for example within a polymer enclosure or wrapping around the anode structure.
  • the protective layer can comprise alumina, in particular applied from a paint or slurry, and/or a polymer.
  • the protective layer may also contain metallic particles that trap a possible oxygen diffusion before it reaches the metallic anode surface.
  • Yet another aspect of the invention relates to an aluminium electrowinning cell comprising at least one oxygen-evolving anode structure as described above.
  • the cell comprises an aluminium-wettable cathode preferably having an aluminium-wettable coating, in particular a drained cathode.
  • aluminium-wettable coatings are disclosed in US Patent 5,651,874 (de Nora/Sekhar ), and PCT publications WO98/17842 (Sekhar/Duruz/Liu ), WO01/42168 (de Nora/Duruz ) and WO01/42531 (Nguyen/Duruz/de Nora ).
  • Suitable drained cathode designs are disclosed in US Patents 5,683,559 , 5,888,360 , 6,093,304 (all de Nora ), 6,258,246 (Duruz/de Nora ), as well as PCT publications WO99/02764 (de Nora/Duruz ), WO99/41429 (de Nora/Duruz ), WO00/63463 (de Nora ), WO01/31086 (de Nora/Duruz ) and WO01/31088 (de Nora ).
  • a prior art-type conditioning of an anode was carried out as follows.
  • An anode was made by pre-oxidising in air at 1100°C for 3 hour a substrate of a cast nickel-iron alloy consisting of 50 weight% nickel, 0.3 weight% manganese, 0.5 weight% aluminium, 0.05 weight% C and 49.15 weight% iron, to form a very thin oxide surface layer on the alloy.
  • the surface-oxidised anode was cut perpendicularly to the anode operative surface and the resulting section of the anode was subjected to microscopic examination.
  • the anode before use had an outer portion that comprised an electrolyte-pervious, electrochemically active iron-rich nickel-iron oxide surface layer having a thickness of up to 10-20 micron and, underneath, an iron-depleted nickel-iron alloy having a thickness of about 10-15 ⁇ m containing generally round cavities filled with iron-rich nickel-iron oxide inclusions and having a diameter of about 2 to 5 ⁇ m.
  • the nickel-iron alloy of the outer portion contained about 75 weight% nickel.
  • the nickel-iron alloy had remained substantially unchanged.
  • An anode prepared as above was pre-heated unprotected in electrolyte fumes above an aluminium electrowinning cell for 20 minutes and then tested therein.
  • the cell contained a molten electrolyte at 880-890°C consisting essentially of NaF and AlF 3 in a weight ratio NaF/AlF 3 of about 0.7 to 0.8, i.e. an excess of AlF 3 in addition to cryolite of about 24 weight% of the electrolyte, and approximately 5 weight% alumina.
  • the alumina concentration was maintained at a substantially constant level throughout the test by adding alumina at a rate adjusted to compensate the cathodic aluminium reduction.
  • the test was run at a current density of about 0.8 A/cm 2 , and the electrical potential of the anode remained in the range of 4.2 to 4.5 volts throughout the test.
  • the anode was cut perpendicularly to the anode operative surface and the resulting section of the used anode was subjected to microscopic examination.
  • anode was covered with an iron oxide surface layer having a thickness of 100 to 120 ⁇ m and consisting essentially of Fe 2 O 3 with less than 5 weight% nickel oxide.
  • An anode was made of the same metals as in the comparative Example except that it had an active surface essentially metallic and free of any ceramic compounds, in particular neither oxides nor fluorides, of metals from the anode's surface.
  • the cold anode was immersed in the molten electrolyte of a cell without prior reaction of the anode's active surface with a reactive environment, i.e. with the active surface essentially metallic and free of said ceramic compounds.
  • the molten electrolyte was at a temperature of 880-890°C and consisted essentially of NaF and AlF 3 in a weight ratio NaF/AlF 3 of about 0.7 to 0.8, i.e. an excess of AlF 3 in addition to cryolite of about 24 weight% of the electrolyte, and approximately 5 weight% alumina.
  • the electrolyte froze around the anode which prevented electrolysis. After 10 to 15 minutes in the electrolyte, the temperature of the anode had reached the melting point of the electrolyte and the electrolyte contacting the anode had molten thereby permitting electrolysis.
  • the alumina concentration was maintained at a substantially constant level throughout the test by adding alumina at a rate adjusted to compensate the cathodic aluminium reduction.
  • the test was run at a current density of about 0.8 A/cm 2 , and the electrical potential of the anode remained in the range of 4.0-4.3 volts throughout the test, i.e. about 0.2 V lower in average than in the above comparative test with a pre-oxidised and fume pre-heated anode.
  • the anode was cut perpendicularly to the anode operative surface and the resulting section of the used anode was subjected to microscopic examination.
  • anode was covered with an iron oxide surface layer having a thickness of about 100 ⁇ m and consisting essentially of Fe 2 O 3 with less than 5 weight% nickel oxide and additionally an outermost layer of oxides of iron and aluminium having a thickness of about 25 ⁇ m.
  • the iron oxide surface layer with pores of 3 to 5 micron, was denser than the oxide layer of the above comparative anode that had pores of 5 to 10 ⁇ m.
  • This greater density of the oxide layer of the anode conditioned according to the invention provides a better protection for the alloy located underneath oxidation and electrolyte attack.
  • Example 1 was repeated with a pre-heating step of the anode above the molten electrolyte prior to immersion into the electrolyte.
  • the anode was covered with a protective layer of alumina applied from an alumina-based colloidal slurry.
  • the colloidal slurry comprised an alumina colloid carrier consisting essentially of water and colloidal alumina particles in an amount of 20 weight% of the colloid, for example Nyacol TM , and suspended alumina particles in an amount of 60 weight% of the colloidal slurry.
  • the anode was dipped into the slurry and allowed to dry to produce an alumina coating having a thickness of 0.6 to 1.0 mm covering and protecting the essentially metallic anode surface against reaction with the environment.
  • the anode After pre-heating the protected anode for about 1 hour in the electrolyte fumes above the molten electrolyte, the anode was immersed with its alumina coating into the molten electrolyte.
  • the protective alumina coating was dissolved almost instantaneously and normal electrolysis could start.
  • the anode behaved like the anode in Example 2. After 24 hours, the anode was removed and examined. The anode upon use was not significantly different to the anode of Example 2.
  • the protective effect of the alumina slurry can be improved by substituting half of the suspended alumina particles with suspended metallic particles, such as aluminium, iron and/or copper particles, which trap a possible oxygen diffusion before it reaches the metallic anode surface.
  • suspended metallic particles such as aluminium, iron and/or copper particles

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Claims (22)

  1. Procédé de conditionnement d'une structure anodique métallique pour produire de l'aluminium dans un électrolyte fondu contenant de l'alumine dissoute, la structure anodique métallique ayant initialement une partie externe en alliage à base fer avec une surface anodique active qui est essentiellement métallique et dépourvue de quelconques composés céramiques, en particulier des oxydes et fluorures, de métaux provenant de la structure anodique métallique, le procédé comprenant les étapes de :
    a) recouvrir la surface active essentiellement métallique dépourvue dudit composé céramique avec une couche protectrice temporaire qui est sensiblement imperméable à une quelconque espèce pouvant réagir avec la surface active pour empêcher sensiblement la surface active de réagir avec une quelconque espèce pouvant réagir, en particulier des espèces oxygène et fluor, jusqu'à l'immersion dans un électrolyte fondu contenant des ions oxygène ;
    b) immerger dans l'électrolyte fondu la structure anodique métallique avec sa surface active essentiellement métallique dépourvue desdits composés céramiques, la couche protectrice temporaire étant éliminée avant l'immersion dans l'électrolyte fondu ou par contact avec l'électrolyte fondu ;
    c) polariser la structure anodique métallique immergée pour former sur celle-ci une couche d'oxyde à base de fer intégrante, dense et cohérente, qui est électrochimiquement active pour l'oxydation de l'oxygène et qui empêche la diffusion de l'oxygène vers la structure anodique métallique.
  2. Procédé de la revendication 1, dans lequel, avant l'immersion, la structure anodique métallique est préchauffée avec sa surface active essentiellement métallique maintenue dépourvue desdits composés céramiques, la couche protectrice étant de préférence stable à la chaleur.
  3. Procédé de la revendication 1 et 2, dans lequel, avant l'immersion, la structure anodique métallique est préchauffée dans une atmosphère qui est sensiblement dépourvue d'une quelconque espèce pouvant réagir avec la surface active.
  4. Procédé d'une quelconque revendication précédente, dans lequel la partie externe en alliage à base de fer comprend du nickel et/ou du cobalt.
  5. Procédé d'une quelconque revendication précédente, dans lequel la partie externe en alliage à base de fer comprend un ou plusieurs éléments choisis parmi le cuivre, le molybdène, le manganèse, le titane, le tantale, le tungstène, l'hafnium, le vanadium, le zirconium, le niobium, le chrome, le cobalt, l'aluminium, le silicium, le carbone et les métaux des terres rares, en particulier l'yttrium.
  6. Procédé de la revendication 4, dans lequel la partie externe en alliage à base de fer se compose essentiellement de :
    - 45-55% en poids de fer ;
    - 15-55 % en poids du total de nickel et/ou de cobalt ;
    - 0-30% en poids de cuivre ; et
    - 0-10% en poids du total d'un ou de plusieurs autres éléments.
  7. Procédé d'une quelconque revendication précédente, dans lequel la structure anodique métallique est un alliage coulé, la structure étant éventuellement trempée avant l'immersion dans l'électrolyte fondu et/ou soumise à un traitement thermique de recuit avant l'immersion dans l'électrolyte fondu.
  8. Procédé de conditionnement ou de reconditionnement d'une structure anodique métallique pour produire de l'aluminium dans un électrolyte fondu contenant de l'alumine dissoute, la structure anodique métallique comprenant une partie externe en alliage à base de fer ayant une surface qui est recouverte de composés céramiques, en particulier des oxydes et des fluorures, de métaux provenant de la partie externe, ledit procédé comprenant les étapes de :
    - éliminer sensiblement tous les composés céramiques de la surface de la partie externe pour former une surface anodique active essentiellement métallique ; et ensuite
    - conditionner selon une quelconque revendication précédente la structure anodique métallique avec sa surface anodique active essentiellement métallique dépourvue de quelconques composés céramiques.
  9. Procédé d'extraction électrolytique d'aluminium comprenant les étapes de :
    - conditionner selon une quelconque revendication précédente une structure anodique métallique incluant l'étape de polarisation dans un électrolyte fondu pour former sur la structure anodique une couche d'oxyde à base de fer intégrante, dense et cohérente ; et
    - électrolyser l'alumine dissoute dans le même électrolyte fondu ou un électrolyte fondu différent en utilisant la structure anodique conditionnée pour dégager de l'oxygène sur celle-ci et produire de l'aluminium sur une cathode en vis-à-vis.
  10. Procédé de la revendication 9, dans lequel la couche d'oxyde à base de fer intégrante, dense et cohérente formée par ladite étape de polarisation du conditionnement est de plus formée pendant l'électrolyse par oxydation lente de la structure anodique métallique au niveau de l'interface structure métallique/couche d'oxyde, éventuellement des constituants de la couche d'oxyde à base de fer intégrante, dense et cohérente se dissolvent lentement dans l'électrolyte pendant l'électrolyse, de préférence à une vitesse correspondant à la vitesse d'oxydation de la structure anodique métallique.
  11. Procédé de la revendication 10, consistant à maintenir dans l'électrolyte fondu de production d'aluminium une quantité suffisante d'espèces de fer dissoutes et d'alumine dissoute pour empêcher la dissolution de façon significative de constituants de la couche d'oxyde à base de fer intégrante, dense et cohérente.
  12. Procédé de l'une quelconque des revendications 9 à 11, consistant à maintenir l'électrolyte fondu de production d'aluminium à une température en dessous de 960°C, de préférence entre 840°C et 940°C.
  13. Procédé de l'une quelconque des revendications 9 à 12, dans lequel l'électrolyte fondu de production d'aluminium contient NaF et AlF3 dans un rapport molaire se trouvant dans la plage de 1,2 à 2,4.
  14. Procédé d'une quelconque des revendications 9 à 13, dans lequel la concentration d'alumine dissoute dans l'électrolyte fondu de production d'aluminium est en dessous de 10% en poids, de préférence entre 5% en poids et 8% en poids.
  15. Procédé d'une quelconque des revendications 9 à 14, dans lequel l'électrolyte appauvri en alumine est mis en circulation au loin de la couche d'oxyde à base de fer électrochimiquement active, est enrichi en alumine, et l'électrolyte enrichi en alumine circule vers la couche d'oxyde à base de fer électrochimiquement active.
  16. Structure anodique d'extraction électrolytique d'aluminium, comprenant une partie externe métallique en alliage à base de fer avec une surface anodique active qui est essentiellement métallique et dépourvue de composés céramiques de métaux provenant de la structure anodique métallique et qui est recouverte d'un milieu de protection temporaire qui empêche sensiblement des réactions formant des céramiques au niveau de la surface anodique essentiellement métallique, lequel milieu peut être séparé de la surface active avant ou lors de l'immersion dans l'électrolyte fondu.
  17. Structure anodique de la revendication 16, dans laquelle le milieu de protection temporaire peut être éliminé avant l'immersion dans l'électrolyte et/ou est soluble dans l'électrolyte.
  18. Structure anodique d'une quelconque des revendications 16 à 17, dans laquelle le milieu de protection temporaire comprend une ou plusieurs couches solides.
  19. Structure anodique de la revendication 18, dans laquelle au moins une couche solide comprend une céramique, telle que l'alumine, et/ou au moins une couche solide comprend un métal, en particulier un métal pouvant réagir, tel que de l'aluminium, du fer, du cuivre, du chrome ou de l'yttrium, pour réagir avec éventuellement des gaz réactifs diffusants.
  20. Structure anodique de la revendication 18 ou 19, dans laquelle au moins une couche solide comprend un polymère, la structure anodique étant éventuellement enroulée sous vide ou sous gaz inerte dans la couche polymère solide.
  21. Structure anodique d'une quelconque ou des revendications 16 à 20, dans laquelle le milieu de protection temporaire comprend : un liquide inerte, tel que de l'huile ou de la graisse ; et/ou un gaz inerte, tel que de l'azote et/ou du dioxyde de carbone.
  22. Cellule d'extraction électrolytique d'aluminium comprenant au moins une structure anodique à dégagement d'oxygène selon la revendication 16 et éventuellement une cathode mouillable par l'aluminium, telle qu'une cathode drainée.
EP03775701A 2002-12-03 2003-12-03 Procede de conditionnement d'anodes a base d'alliage de fer pour des cellules d'extraction electrolytique d'aluminium Expired - Lifetime EP1567692B1 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
IB0205112 2002-12-03
WOPCT/IB02/05112 2002-12-03
PCT/IB2003/005713 WO2004050956A1 (fr) 2002-12-03 2003-12-03 Procede de conditionnement d'anodes a base d'alliage de fer pour des cellules d'extraction electrolytique d'aluminium

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EP1567692A1 EP1567692A1 (fr) 2005-08-31
EP1567692B1 true EP1567692B1 (fr) 2007-11-21

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US (1) US20060151334A1 (fr)
EP (1) EP1567692B1 (fr)
AU (1) AU2003283720A1 (fr)
CA (1) CA2503131A1 (fr)
DE (1) DE60317703D1 (fr)
NO (1) NO20053249L (fr)
NZ (1) NZ539705A (fr)
WO (1) WO2004050956A1 (fr)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3861938A (en) * 1972-03-13 1975-01-21 Int Nickel Co Protective coating for metals
US5069929A (en) * 1984-09-19 1991-12-03 Sumitomo Metal Industries, Ltd. Actinic radiation-curable rust-preventive coating compositions for steel products
DE4400391A1 (de) * 1994-01-08 1995-07-13 Messer Griesheim Gmbh Verfahren zur Vermeidung von Randoxidation beim Aufkohlen von Stählen
US5904828A (en) * 1995-09-27 1999-05-18 Moltech Invent S.A. Stable anodes for aluminium production cells
US6248227B1 (en) * 1998-07-30 2001-06-19 Moltech Invent S.A. Slow consumable non-carbon metal-based anodes for aluminium production cells
AU4794699A (en) * 1998-07-30 2000-02-21 Moltech Invent S.A. Slow consumable non-carbon metal-based anodes for aluminium production cells
AU1404100A (en) * 1999-12-09 2001-06-18 Moltech Invent S.A. Aluminium electrowinning cells operating with metal-based anodes
US20050000823A1 (en) * 2001-08-06 2005-01-06 Nguyen Thinh T. Aluminium production cells with iron-based metal alloy anodes

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CA2503131A1 (fr) 2004-06-17
AU2003283720A1 (en) 2004-06-23
NO20053249L (no) 2005-07-01
US20060151334A1 (en) 2006-07-13
DE60317703D1 (de) 2008-01-03
WO2004050956A1 (fr) 2004-06-17
NZ539705A (en) 2007-04-27
EP1567692A1 (fr) 2005-08-31

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