EP0322326B1 - Protective coating for studs and emerging parts of prebaked anodes - Google Patents

Protective coating for studs and emerging parts of prebaked anodes Download PDF

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Publication number
EP0322326B1
EP0322326B1 EP19880420430 EP88420430A EP0322326B1 EP 0322326 B1 EP0322326 B1 EP 0322326B1 EP 19880420430 EP19880420430 EP 19880420430 EP 88420430 A EP88420430 A EP 88420430A EP 0322326 B1 EP0322326 B1 EP 0322326B1
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Prior art keywords
anodes
alumina
anode
logs
protective coating
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EP19880420430
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German (de)
French (fr)
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EP0322326A1 (en
Inventor
Gabriel Audras
Bernard Samanos
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Carbone Savoie SAS
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Societe des Electrodes et Refractaires Savoie SA
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Priority claimed from FR878718452A external-priority patent/FR2624886B2/en
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C3/00Electrolytic production, recovery or refining of metals by electrolysis of melts
    • C25C3/06Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
    • C25C3/08Cell construction, e.g. bottoms, walls, cathodes
    • C25C3/12Anodes
    • C25C3/125Anodes based on carbon
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C7/00Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
    • C25C7/02Electrodes; Connections thereof
    • C25C7/025Electrodes; Connections thereof used in cells for the electrolysis of melts

Definitions

  • the invention relates to a coating for protection against corrosion and hot oxidation for pre-baked anode logs and the emerging carbonaceous part of these anodes used in aluminum production tanks by electrolysis of alumina dissolved in the cryolite melted using the Hall-Héroult process.
  • anode plugs are introduced into the upper part of the anode, into which logs (or steel plates) will be introduced and sealed. ) which will serve both to suspend the anode from the anode frame and to supply it with current.
  • the sealing is carried out by casting iron or more rarely by means of a carbonaceous paste of special composition.
  • the steel logs are subjected both to a high temperature and to the corrosive effect of the fluorinated effluents emitted by the tank in operation.
  • the molten cryolithic bath can come into contact with the base. steel logs.
  • the emerging part of the anodes that is to say the upper part which, in normal operation of the electrolytic cell, is not immersed in the molten electrolyte, undergoes degradation by combustion, that l 'It is sought to avoid by covering a solidified and ground electrolysis bath, possibly mixed with alumina, or by metallization obtained by spraying liquid aluminum.
  • SERS European patent application EP 0 269 534
  • This composition is essentially characterized by a carbon aggregate such as coke, artificial graphite, waste anodes or semi-graphite electrodes with a low ash content (preferably ⁇ 2%) bound by a lime aluminate cement, to low content of annoying impurities (SiO2, Fe2O3, TiO2, K2O, Cr2O3, total content preferably less than 1%) having an alumina content at least equal to 70% and, preferably, at least equal to 80%, the together being linked by addition of water.
  • a carbon aggregate such as coke, artificial graphite, waste anodes or semi-graphite electrodes with a low ash content (preferably ⁇ 2%) bound by a lime aluminate cement, to low content of annoying impurities (SiO2, Fe2O3, TiO2, K2O, Cr2O3, total content preferably less than 1%) having an alumina content at least equal to 70% and, preferably, at least equal to 80%, the together being linked by addition of water.
  • a complementary addition of magnesium spinel (Al2O3, MgO), whose thermal conductivity is high, makes it possible to lower the temperature of the surface of the anode, thus delaying oxidation.
  • alumina for example alumina for electrolysis or globular alumina, at a content which can constitute up to 50% of the total weight of the aggregate.
  • the cement content by weight, expressed in weight percent of the aggregate (carbon product + additives) is between 10 and 60% and, preferably, from 15 to 50%. It is appropriate to denote by "dry matter” the whole of the aggregate (carbonaceous product, alumina, additives) and the cement.
  • the same compositions are suitable, but it is then preferable to apply them by spraying with a gun.
  • a gun it is necessary, depending on the type of gun used, to control the particle size of the aggregate and the cement (less than 1 mm and, preferably, less than 0.5 mm) and significantly increase the quantity of water.
  • This amount of water will be fixed, for example, between 10 and 70% by weight relative to the dry matter (as defined above) for use in the form of collar paste and, up to 60% by weight for use in the form of a fluid paste to be sprayed on with a spray gun.
  • the object of the present invention is a protective composition which does not have the drawbacks of carbonaceous pastes or comprising a carbonaceous aggregate, and which provides effective protection of the base of the steel logs and possibly of the carbonaceous part emerging from the anodes throughout the lifespan of the anodes (about twenty days on average).
  • This composition is characterized by a mixture of dry materials made up of lime aluminate cement, magnesium spinel, possibly fine powdered alumina and water.
  • the lime aluminate cement has an alumina content of at least 70% and preferably 80% by weight. It preferably contains less than 1% of annoying impurities (SiO2, Fe2O3, TiO2, K2O, Cr2O3)
  • composition of the dry matter mixture is located in the following ranges:
  • the amount of water is between 10 and 80% of the total weight of the dry matter, the contents between 10 and about 50% corresponding to a pasty composition, usable as flange paste, and the contents going up to 80% corresponding to a fluid paste usable by spraying with a gun, with, in this case, a particle size of the dry materials less than 1 mm and preferably less than 0.5 mm.
  • the protective coating of the emerging part of prebaked anodes was implemented according to three formulations for application by spraying with a spray gun, which is adapted - by reducing the water content - for the use of paste paste.
  • the carbon substrate for the tests consists of a core 30 mm in diameter and 120 mm high.
  • the different compositions A, B, C are applied to a group of samples and a certain number of controls are kept without coating. All the samples are treated for 1 hour at 1000 ° C. under nitrogen to remove all traces of water.
  • a 2 hour carboxyreactivity test is then carried out at 1000 ° C. under a CO2 flow rate of 50 liters / hour.
  • the samples are cooled under a stream of nitrogen and each carrot is weighed to determine its weight loss.
  • the results are expressed in milligrams related to an area of 1 cm2 and for a duration of 1 hour. The result is therefore given in mg.cm ⁇ 2.h ⁇ 1.
  • the following results were obtained:
  • the optimal compositions expressed in Secar Cement / Secar cement + Al2O3 + Spinel ratio being between 5 and 50%.
  • the percentage of water to be added depends on the cement content and the particle size of the alumina. It is between 30 and 50 and preferably between 35 and 45% by weight relative to dry matter (that is to say 35 to 45 grams of water per 100 grams of the mixture of Secar cement + alumina + magnesium spinel ).
  • the reduction in corrosion of the anode logs is evident from the first cycle and is accentuated during the following cycles. It can be estimated that the useful life of the anode logs is extended by at least 30%.
  • Secar cement based on calcium aluminate having an alumina content at least equal to 70% and preferably at least equal to 80%.
  • the composition of Secar 80 and 71 cements from the company LAFARGE FONDU INTERNATIONAL and Spinel of Magnesium, from PEM (PECHINEY ELECTROMETALLURGY) are recalled below:

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Metals (AREA)
  • Prevention Of Electric Corrosion (AREA)
  • Furnace Housings, Linings, Walls, And Ceilings (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)

Description

DOMAINE TECHNIQUE DE L'INVENTIONTECHNICAL FIELD OF THE INVENTION

L'invention concerne un revêtement de protection contre la corrosion et l'oxydation à chaud destiné aux rondins d'anodes précuites et à la partie carbonée émergeante de ces anodes utilisées dans les cuves de production d'aluminium par électrolyse d'alumine dissoute dans de la cryolithe fondue selon le procédé Hall-Héroult.The invention relates to a coating for protection against corrosion and hot oxidation for pre-baked anode logs and the emerging carbonaceous part of these anodes used in aluminum production tanks by electrolysis of alumina dissolved in the cryolite melted using the Hall-Héroult process.

ETAT DE LA TECHNIQUESTATE OF THE ART

La plupart des cuves modernes pour la production électrolytique selon le procédé Hall-Héroult utilisent des anodes carbonées dites "précuites" obtenues par mise en forme à 120-160°C environ d'une pâte carbonée essentiellement constituée de coke (et/ou anthracite) et de brai, puis cuisson pendant une centaine d'heures à 1150/1200°C.Most modern tanks for electrolytic production according to the Hall-Héroult process use carbonaceous anodes called "precooked" obtained by shaping at around 120-160 ° C a carbonaceous paste essentially consisting of coke (and / or anthracite) and pitch, then baking for a hundred hours at 1150/1200 ° C.

Lors de la mise en forme de la pâte, on ménage, à la partie supérieure de l'anode, un certain nombre de cavités souvent appelées "bouchons d'anode" dans lesquelles on introduira et scellera des rondins (ou des plaques d'aciers) qui serviront à la fois à suspendre l'anode au cadre anodique et à l'alimenter en courant. Le scellement est effectué par coulée de fonte ou plus rarement au moyen d'une pâte carbonée de composition spéciale.During the shaping of the dough, a number of cavities, often called "anode plugs", are introduced into the upper part of the anode, into which logs (or steel plates) will be introduced and sealed. ) which will serve both to suspend the anode from the anode frame and to supply it with current. The sealing is carried out by casting iron or more rarely by means of a carbonaceous paste of special composition.

Les rondins d'acier sont soumis à la fois à une température élevée et à l'effet corrosif des effluents fluorés émis par la cuve en fonctionnement. En outre, lors de certaines opérations, par exemple lors d'une descente d'anodes destinée à faire cesser un "effet anodique", ou lors de "vagues" dans l'électrolyte, du bain cryolithique fondu peut entrer en contact avec la base des rondins d'acier.The steel logs are subjected both to a high temperature and to the corrosive effect of the fluorinated effluents emitted by the tank in operation. In addition, during certain operations, for example during an anode descent intended to stop an "anodic effect", or during "waves" in the electrolyte, the molten cryolithic bath can come into contact with the base. steel logs.

Ces diverses causes font que la teneur en fer de l'aluminium produit dans la cuve est sensiblement augmentée par la corrosion de base des rondins. Cette corrosion a aussi pour effet nocif de réduire la durée de vie de l'ensemble de suspension des anodes (rondins + barres de liaison entre les rondins et la tige d'anode) qui sont normalement récupérés et réutilisés après extraction de la cuve des anodes uséesThese various causes cause the iron content of the aluminum produced in the tank to be appreciably increased by the basic corrosion of the logs. This corrosion also has the harmful effect of reducing the service life of the anode suspension assembly (logs + connecting bars between the logs and the anode rod) which are normally recovered and reused. after extraction of the spent anode tank

De même, la partie émergeante des anodes, c'est-à-dire la partie supérieure qui, en fonctionnement normal de la cuve d'électrolyse, n'est pas immergée dans l'électrolyte fondu, subit une dégradation par combustion, que l'on cherche à éviter par un recouvrement de bain d'électrolyse solidifié et broyé, éventuellement mélangé d'alumine, ou encore par une métallisation obtenue par projection d'aluminium liquide.Similarly, the emerging part of the anodes, that is to say the upper part which, in normal operation of the electrolytic cell, is not immersed in the molten electrolyte, undergoes degradation by combustion, that l 'It is sought to avoid by covering a solidified and ground electrolysis bath, possibly mixed with alumina, or by metallization obtained by spraying liquid aluminum.

On a également cherché à protéger la base des rondins par différents procédés tels que la métallisation par projection d'aluminium liquide ou la mise en place, autour des rondins, d'une collerette en aluminium laissant avec le rondin (ou la plaque) un espace de 10 à 30 mm que l'on remplit d'une pâte carbonée coulée à chaud. On a proposé pour cela des pâtes carbonées classiques (coke et/ou anthracite et/ou graphite + brai) ou des compositions plus complexes comportant des produits organiques polymérisables et cokéfiables tels que résines époxy, résines furfuryliques, etc... (demande de brevet allemand DE-AS 25 47 061).We have also sought to protect the base of the logs by various methods such as metallization by projection of liquid aluminum or the installation, around the logs, of an aluminum flange leaving with the log (or the plate) a space from 10 to 30 mm which is filled with a carbonaceous paste poured hot. For this, conventional carbonaceous pastes (coke and / or anthracite and / or graphite + pitch) have been proposed or more complex compositions comprising polymerizable and coking organic products such as epoxy resins, furfuryl resins, etc. (patent application German DE-AS 25 47 061).

Toutefois, ces compositions hydrocarbonées ont pour inconvénient majeur de provoquer, dès la mise en service de l'anode, qui atteint progressivement sa température d'équilibre, un dégagement de vapeurs d'hydrocarbures provenant du craquage de la pâte carbonée. Certains composés aromatiques ainsi formés sont soupçonnés d'effets physiologiques néfastes, et, en outre, ils polluent et favorisent l'obstruction des circuits d'aspiration et de lavage d'effluents sur les cuves d'électrolyse. Pour toutes ces raisons, les "pâtes de collerettes" composées uniquement de produits carbonés ne satisfont plus les exploitants de cuves d'électrolyse à anodes précuites. Or, la tendance actuelle est, précisément, de produire dans les cuves un aluminium primaire de pureté aussi élevée que possible. La corrosion de la base des rondins étant une des sources de fer dans l'aluminium produit, il importait donc de trouver un moyen de protection efficace et qui, de préférence, s'applique également à la partie carbonée émergeante des anodes.However, these hydrocarbon compositions have the major drawback of causing, as soon as the anode is put into service, which gradually reaches its equilibrium temperature, a release of hydrocarbon vapors from the cracking of the carbonaceous paste. Certain aromatic compounds thus formed are suspected of harmful physiological effects, and, in addition, they pollute and favor the obstruction of the suction and washing circuits of effluents on the electrolytic cells. For all these reasons, "flange pastes" composed solely of carbonaceous products no longer satisfy the operators of electrolysis tanks with prebaked anodes. However, the current trend is, precisely, to produce in the primary primary aluminum of as high a purity as possible. Corrosion of the base of the logs being one of the sources of iron in the aluminum produced, it was therefore important to find an effective means of protection which, preferably, also applies to the carbonaceous part emerging from the anodes.

La demande de brevet européen EP 0 269 534 (SERS) a pour objet une composition de pâte de collerette ne présentant pas les inconvénients des pâtes carbonées, et assurant une protection efficace de la base des rondins d'acier et éventuellement de la partie carbonée émergeante des anodes pendant toute la durée de vie des anodes (soit une vingtaine de jours en moyenne). Cette composition est essentiellement caractérisée par un agrégat carboné tel que coke, graphite artificiel, déchets d'anodes ou d'électrodes semi-graphite à faible teneur en cendre (de préférence < 2%) lié par un ciment d'aluminate de chaux, à faible teneur en impuretés gênantes (SiO₂, Fe₂O₃, TiO₂, K₂O, Cr₂O₃, teneur totale de préférence inférieure à 1%) ayant une teneur en alumine au moins égale à 70% et, de préférence, au moins égale à 80%, l'ensemble étant lié par addition d'eau.The subject of European patent application EP 0 269 534 (SERS) is a flange paste composition which does not have the drawbacks of carbonaceous pastes, and which provides effective protection of the base of the steel logs and possibly of the carbonaceous part emerging from the anodes during the entire life of the anodes (about twenty days on average). This composition is essentially characterized by a carbon aggregate such as coke, artificial graphite, waste anodes or semi-graphite electrodes with a low ash content (preferably <2%) bound by a lime aluminate cement, to low content of annoying impurities (SiO₂, Fe₂O₃, TiO₂, K₂O, Cr₂O₃, total content preferably less than 1%) having an alumina content at least equal to 70% and, preferably, at least equal to 80%, the together being linked by addition of water.

Ces impuretés sont qualifiées de gênantes car, introduites dans le bain d'électrolyse, elles sont réduites et les métaux correspondants Si, Fe, Ti, Cr, Mn, K s'allient à l'aluminium liquide.These impurities are classified as troublesome because, introduced into the electrolysis bath, they are reduced and the corresponding metals Si, Fe, Ti, Cr, Mn, K are combined with liquid aluminum.

Une addition complémentaire de spinelle de magnésium (Al₂O₃, MgO), dont la conductivité thermique est élevée, permet d'abaisser la température de la surface de l'anode, retardant ainsi l'oxydation.A complementary addition of magnesium spinel (Al₂O₃, MgO), whose thermal conductivity is high, makes it possible to lower the temperature of the surface of the anode, thus delaying oxidation.

On peut également effectuer dans la pâte une addition d'alumine, par exemple de l'alumine pour électrolyse ou de l'alumine globulaire, à une teneur pouvant constituer jusqu'à 50 % du poids total de l'agrégat.It is also possible to add alumina to the paste, for example alumina for electrolysis or globular alumina, at a content which can constitute up to 50% of the total weight of the aggregate.

La teneur pondérale en ciment, exprimée en pour-cent en poids de l'agrégat (produit carboné+additifs) est comprise entre 10 et 60 % et, de préférence, de 15 à 50 %. On convient de désigner par "matière sèche" l'ensemble de l'agrégat (produit carboné, alumine, additifs) et du ciment.The cement content by weight, expressed in weight percent of the aggregate (carbon product + additives) is between 10 and 60% and, preferably, from 15 to 50%. It is appropriate to denote by "dry matter" the whole of the aggregate (carbonaceous product, alumina, additives) and the cement.

Pour la protection de la partie émergeante de l'anode, les mêmes compositions conviennent, mais il est alors préférable de les appliquer par projection au pistolet. Pour cela, il est nécessaire, en fonction du type de pistolet utilisé, de contrôler la granulométrie de l'agrégat et du ciment (inférieure à 1 mm et, de préférence, inférieure à 0,5 mm) et d'augmenter sensiblement la quantité d'eau.For the protection of the emerging part of the anode, the same compositions are suitable, but it is then preferable to apply them by spraying with a gun. For this, it is necessary, depending on the type of gun used, to control the particle size of the aggregate and the cement (less than 1 mm and, preferably, less than 0.5 mm) and significantly increase the quantity of water.

Cette quantité d'eau sera fixée, par exemple, entre 10 et 70 % en poids par rapport à la matière sèche (telle que définie ci-dessus) pour l'utilisation sous forme de pâte de collerette et, jusqu'à 60% en poids pour l'utilisation sous forme de pâte fluide à projeter au pistolet.This amount of water will be fixed, for example, between 10 and 70% by weight relative to the dry matter (as defined above) for use in the form of collar paste and, up to 60% by weight for use in the form of a fluid paste to be sprayed on with a spray gun.

OBJET DE LA PRESENTE INVENTIONOBJECT OF THE PRESENT INVENTION

L'objet de la présente invention est une composition de protection ne présentant pas les inconvénients des pâtes carbonées ou comportant un agrégat carboné, et assurant une protection efficace de la base des rondins d'acier et éventuellement de la partie carbonée émergeante des anodes pendant toute la durée de vie des anodes (soit une vingtaine de jours en moyenne). Cette composition est caractérisée par un mélange de matières sèches constituées de ciment d'aluminate de chaux, de spinelle de magnésium, éventuellement d'alumine en poudre fine et d'eau.The object of the present invention is a protective composition which does not have the drawbacks of carbonaceous pastes or comprising a carbonaceous aggregate, and which provides effective protection of the base of the steel logs and possibly of the carbonaceous part emerging from the anodes throughout the lifespan of the anodes (about twenty days on average). This composition is characterized by a mixture of dry materials made up of lime aluminate cement, magnesium spinel, possibly fine powdered alumina and water.

Le ciment d'aluminate de chaux a une teneur en alumine égale au moins à 70 % et de préférence à 80% en poids. Il contient de préférence moins de 1 % d'impuretés gênantes (SiO₂, Fe₂O₃, TiO₂, K₂O, Cr₂O₃)The lime aluminate cement has an alumina content of at least 70% and preferably 80% by weight. It preferably contains less than 1% of annoying impurities (SiO₂, Fe₂O₃, TiO₂, K₂O, Cr₂O₃)

La composition du mélange de matières sèches est située dans les intervalles suivants :

Figure imgb0001
The composition of the dry matter mixture is located in the following ranges:
Figure imgb0001

La quantité d'eau se situe entre 10 et 80% du poids total des matières sèches, les teneurs entre 10 et environ 50 % correspondant à une composition pâteuse, utilisable comme pâte de collerette, et les teneurs allant jusqu'à 80% correspondant à une pâte fluide utilisable par projection au pistolet, avec, dans ce cas, une granulométrie des matières sèches inférieure à 1mm et de préférence inférieure à 0,5 mm.The amount of water is between 10 and 80% of the total weight of the dry matter, the contents between 10 and about 50% corresponding to a pasty composition, usable as flange paste, and the contents going up to 80% corresponding to a fluid paste usable by spraying with a gun, with, in this case, a particle size of the dry materials less than 1 mm and preferably less than 0.5 mm.

DESCRIPTION DE L'INVENTIONDESCRIPTION OF THE INVENTION Cas de la protection de la partie émergeante des anodesProtection of the emerging part of the anodes

Le revêtement protecteur de la partie émergeante d'anodes précuites a été mis en oeuvre selon trois formulations pour application par pulvérisation au pistolet, que l'on adapte - en diminuant la teneur en eau - pour l'utilisation en pâte de collerettes.

Figure imgb0002
The protective coating of the emerging part of prebaked anodes was implemented according to three formulations for application by spraying with a spray gun, which is adapted - by reducing the water content - for the use of paste paste.
Figure imgb0002

Les conditions de pulvérisation ont été les suivantes : le substrat carboné pour les tests est constitué par une carotte de 30 mm de diamètre et de 120 mm de haut.
On applique les différentes compositions A,B,C sur un groupe d'échantillons et on conserve un certain nombre de témoins sans revêtement. L'ensemble des échantillons est traité 1 heure à 1000°C sous azote pour enlever toute trace d'eau. On effectue ensuite un test de carboxyréactivité de 2 heures à 1000°C sous un débit de CO₂ de 50 litres/heure. En fin de test, on refroidit les échantillons sous courant d'azote et on pèse chaque carotte pour déterminer sa perte de poids. Les résultats sont exprimés en milligrammes rapportés à une surface de 1 cm² et à une durée de 1 heure. Le résultat est donc donné en mg.cm⁻².h⁻¹.
On a obtenu les résultats suivants :

Figure imgb0003
The spraying conditions were as follows: the carbon substrate for the tests consists of a core 30 mm in diameter and 120 mm high.
The different compositions A, B, C are applied to a group of samples and a certain number of controls are kept without coating. All the samples are treated for 1 hour at 1000 ° C. under nitrogen to remove all traces of water. A 2 hour carboxyreactivity test is then carried out at 1000 ° C. under a CO₂ flow rate of 50 liters / hour. At the end of the test, the samples are cooled under a stream of nitrogen and each carrot is weighed to determine its weight loss. The results are expressed in milligrams related to an area of 1 cm² and for a duration of 1 hour. The result is therefore given in mg.cm⁻².h⁻¹.
The following results were obtained:
Figure imgb0003

On note l'efficacité particulière des formulations A et B qui réduisent la réactivité au CO₂ de près de 25 % .Note the particular effectiveness of formulations A and B which reduce the reactivity to CO₂ by almost 25%.

Des tests de longue durée ont été effectués en condition industrielle, sur la partie émergeante des anodes d'un certain nombre de cuves d'électrolyse Hall-Héroult. Les résultats sont moins précis du fait que les mégots d'anodes usées sont après leur retrait de la cuve, enrobés de bain d'électrolyse dont la séparation n'est jamais parfaite, mais ils confirment l'ordre de grandeur de 25% de diminution de l'oxydation de la partie émergeante des anodes précuites.Long-term tests were carried out under industrial conditions, on the emerging part of the anodes of a number of Hall-Héroult electrolysis cells. The results are less precise since the spent anode butts are coated with an electrolysis bath after their removal from the tank, the separation of which is never perfect, but they confirm the order of magnitude of 25% reduction. oxidation of the emerging part of the prebaked anodes.

Cas de la protection des rondins d'anodes précuitesProtection of pre-baked anode logs

Pour la protection des rondins d'anodes, le revêtement protecteur est mis en place à l'état de pâte. Les conditions de corrosion en cours d'électrolyse étant difficiles à simuler, on a procédé aux tests en conditions réelles, par mesure de la diminution du diamètre des rondins après extraction des anodes usées (soit après environ 3 semaines de séjour dans la cuve d'électrolyse).
Les compositions, pour cet usage, sont comprises dans les limites suivantes:

Ciment
: 10 à 95 %
Alumine
: 0 à 80 %
Spinelle de Mg
: 5 à 10 %
To protect the anode logs, the protective coating is placed in the paste state. The corrosion conditions during electrolysis being difficult to simulate, the tests were carried out under real conditions, by measuring the reduction in the diameter of the logs after extraction of the used anodes (ie after approximately 3 weeks of stay in the electrolysis).
The compositions for this use are included within the following limits:
Cement
: 10 to 95%
Alumina
: 0 to 80%
Mg Spinel
: 5 to 10%

Les compositions optimales exprimées en rapport Ciment Secar/ciment Secar+Al₂O₃+Spinelle étant situées entre 5 et 50%. Le pourcentage d'eau à ajouter dépend de la teneur en ciment et de la granulométrie de l'alumine. Il se situe entre 30 et 50 et de préférence entre 35 et 45% en poids par rapport aux matières sèches (c'est-à-dire 35 à 45 grammes d'eau pour 100 grammes du mélange ciment Secar + alumine + spinelle de magnésium). La diminution de corrosion des rondins d'anode est évidente dès le premier cycle et s'accentue au cours des cycles suivants. On peut estimer que la durée de vie utile des rondins d'anodes est prolongée d'au moins 30 %.The optimal compositions expressed in Secar Cement / Secar cement + Al₂O₃ + Spinel ratio being between 5 and 50%. The percentage of water to be added depends on the cement content and the particle size of the alumina. It is between 30 and 50 and preferably between 35 and 45% by weight relative to dry matter (that is to say 35 to 45 grams of water per 100 grams of the mixture of Secar cement + alumina + magnesium spinel ). The reduction in corrosion of the anode logs is evident from the first cycle and is accentuated during the following cycles. It can be estimated that the useful life of the anode logs is extended by at least 30%.

Bien que l'invention ait été décrite dans le cas particulier de l'utilisation de ciment Secar, elle s'applique de la même façon avec tout ciment à base d'aluminate de calcium ayant une teneur en alumine au moins égale à 70% et de préférence au moins égale à 80%. On rappelle ci-après la composition des ciments Secar 80 et 71 de la Société LAFARGE FONDU INTERNATIONAL et du Spinelle de Magnésium, de PEM (PECHINEY ELECTROMETALLURGIE):

Figure imgb0004
Although the invention has been described in the particular case of the use of Secar cement, it applies in the same way with any cement based on calcium aluminate having an alumina content at least equal to 70% and preferably at least equal to 80%. The composition of Secar 80 and 71 cements from the company LAFARGE FONDU INTERNATIONAL and Spinel of Magnesium, from PEM (PECHINEY ELECTROMETALLURGY) are recalled below:
Figure imgb0004

Claims (2)

1. A coating for affording protection from corrosion and oxidation in the hot condition of the carrier bars of prebaked anodes and the emerging part of such anodes which are intended for the electrolysis tanks for the production of aluminium using the Hall-Heroult process, characterised in that it is formed by a mixture of dry materials composed of calcium aluminate having an alumina a content of at least equal to 70%, with a low proportion of troublesome impurities, magnesian spinel, and optionally alumina in the form of fine powder, in the following proportions by weight:
calcium aluminate cement   : 10 to 95%
alumina in powder form   : 0 to 80%
magnesian spinel   : 5 to 10%
bound with water in a proportion of from 10 to 80% of the total weight of the dry materials.
2. A protective coating according to claim 1 characterised in that, for application in the form of a collar portion paste to anode carrier bars, the composition is preferably within the following limits: dry materials (calcium aluminate cement)
Figure imgb0007
EP19880420430 1987-12-22 1988-12-21 Protective coating for studs and emerging parts of prebaked anodes Expired - Lifetime EP0322326B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR878718452A FR2624886B2 (en) 1986-11-14 1987-12-22 IMPROVEMENT IN PROTECTIVE COATINGS FOR PRE-COOKED ANODES AND THE EMERGING PART OF THESE ANODES
FR8718452 1987-12-22

Publications (2)

Publication Number Publication Date
EP0322326A1 EP0322326A1 (en) 1989-06-28
EP0322326B1 true EP0322326B1 (en) 1992-08-12

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EP19880420430 Expired - Lifetime EP0322326B1 (en) 1987-12-22 1988-12-21 Protective coating for studs and emerging parts of prebaked anodes

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AU (1) AU610964B2 (en)
BR (1) BR8806778A (en)
CA (1) CA1340408C (en)
DE (1) DE3873713T2 (en)
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IN (1) IN169360B (en)
IS (1) IS1465B6 (en)
NO (1) NO885645L (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2606796B1 (en) * 1986-11-14 1989-02-03 Savoie Electrodes Refract PROTECTIVE COATING FOR PRE-COOKED ANODE ROUND
NO930957L (en) * 1993-03-17 1994-09-19 Norsk Hydro As Marterial composite for oxidation and corrosion protection of anode nipples
US6818106B2 (en) * 2002-01-25 2004-11-16 Alcoa Inc. Inert anode assembly
WO2004035870A1 (en) * 2002-10-18 2004-04-29 Moltech Invent S.A. Anode current feeding connection stem
ES2644864T3 (en) * 2002-11-25 2017-11-30 Alcoa Inc. Inert Anode Assembly

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1365820A (en) * 1972-02-15 1974-09-04 Zirconal Processes Ltd Coating composition suitable for use at high temperatures
FR2411166A1 (en) * 1977-12-12 1979-07-06 Lafarge Fondu Int REFRACTORY HYDRAULIC BINDER BASED ON CALCIUM ALUMINATE AND ITS PREPARATION PROCESS
US4354918A (en) * 1981-01-14 1982-10-19 Martin Marietta Corporation Anode stud coatings for electrolytic cells
JPS61111983A (en) * 1984-11-02 1986-05-30 ミサワホ−ム株式会社 Manufacture of foamed concrete
BR8500347A (en) * 1985-01-25 1986-09-09 Ardal Og Sunndal Verk PRE-COOKED ANODE WITH REDUCED CARBON LOSS FOR EMPLOYMENT IN ALUMINUM PRODUCTION BY REDUCTION BY ELECTROLYTIC FUSION AND THE PROCESS TO PRODUCE THE SAME

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NO885645L (en) 1989-06-23
DE3873713D1 (en) 1992-09-17
NO885645D0 (en) 1988-12-20
IN169360B (en) 1991-09-28
EP0322326A1 (en) 1989-06-28
CA1340408C (en) 1999-02-23
BR8806778A (en) 1989-08-29
IS1465B6 (en) 1991-03-26
AU610964B2 (en) 1991-05-30
ES2043877T3 (en) 1994-01-01
IS3424A7 (en) 1989-06-23
DE3873713T2 (en) 1993-02-11
AU2742988A (en) 1989-06-22

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