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EP1080243B1 - Low pressure carbonitriding method for metal alloy parts - Google Patents

Low pressure carbonitriding method for metal alloy parts Download PDF

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Publication number
EP1080243B1
EP1080243B1 EP99915850A EP99915850A EP1080243B1 EP 1080243 B1 EP1080243 B1 EP 1080243B1 EP 99915850 A EP99915850 A EP 99915850A EP 99915850 A EP99915850 A EP 99915850A EP 1080243 B1 EP1080243 B1 EP 1080243B1
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Prior art keywords
nitrogen
action
metal alloy
ammonia
nitriding gas
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German (de)
French (fr)
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EP1080243A1 (en
Inventor
Jacques Frey
Philippe Dubois
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Aubert and Duval SA
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Aubert and Duval SA
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C8/00Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C8/06Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases
    • C23C8/28Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases more than one element being applied in one step
    • C23C8/30Carbo-nitriding
    • C23C8/32Carbo-nitriding of ferrous surfaces

Definitions

  • the subject of the present invention is a carbonitriding process of alloy parts metallic.
  • Carbonitriding is a thermochemical treatment of simultaneous diffusion of carbon and nitrogen from the surface of a ferrous alloy in the solid state. It is generally carried out in a sealed oven, in which a controlled atmosphere is maintained, consisting of a support gas to which is added if necessary, to achieve the desired carbon potential, a carbon enrichment gas, and in addition, a nitrogen gas.
  • the support gas is an endothermic generator gas comprising an alkane which is oxidized to carbon monoxide CO, since oxidation is carried out in the absence of air with respect to the stoichiometric reaction which would transform all the carbon into CO 2 .
  • the gases used can be nitrogen-methanol mixtures or endothermic mixtures based on hydrocarbon and ammonia, as described in “The Engineering Techniques, M1226-8 to 14, July 1994, [1].
  • the conventional method implements atmospheres that all contain oxygen the presence or formation of CO.
  • Oxygen released by the decomposition of CO leads to oxidation surface of the steel which, on the one hand, brakes absorption of carbon and, on the other hand, leads to harmful structures in terms of characteristics mechanical of the treated part, contact fatigue by example.
  • the carbonitrided parts that way are most often used in the state, without any mechanical touch-up of the surface.
  • the subject of the present invention is a carbonitriding process which avoids the harmful presence of oxygen during treatment thermochemical diffusion of carbon and nitrogen in the metal alloy part.
  • the method of carbonitriding of metal alloy parts consists in subjecting said documents to the action of a fuel mixture consisting of ethylene and hydrogen, and the action of a nitriding gas consisting of ammonia, under a pressure of less than 100 hPa and at a temperature from about 750 to about 1050 ° C.
  • the supply of carbon is made by the direct dissociation of a hydrocarbon, in this case ethylene, in the enclosure of a vacuum furnace, and the supply of nitrogen comes from the dissociation.
  • a hydrocarbon in this case ethylene
  • nitrogen comes from the dissociation.
  • ammonia gas depending on the thermally activated reaction: 2NH 3 ⁇ N 2 + 3H 2 .
  • this carbonitriding temperatures treatment more higher than those usually used for this type of reaction, which were usually in a range from 400 to 600 ° C.
  • the dissociation reaction of ammonia is thermodynamically total, but its kinetics is weak. As a result, it still exists at level of the ammonia part to be dissociated, generating active nascent nitrogen. It is for this reason that ammonia can be used for nitrogen supply.
  • the pressure used can be particularly in the range of 10 to 100 hPa.
  • One of the other advantages of the invention is to be able to enrich the surface of the carbon and nitrogen part in a range of much wider temperature, from around 750 to around 1050 ° C, depending on the enrichment sequences considered.
  • the use of the reaction of dissociation of ethylene at low pressure allows be able to provide carbon from 750 ° C and thus lowering the temperature to benefit from a power nitriding more important ammonia because the availability of atomic nitrogen useful for diffusion, is greater. This increases the possibilities for surface carbon enrichment and in nitrogen.
  • the carbonitriding either by subjecting said parts to the simultaneous action of the fuel and gas mixture nitriding, either by subjecting said parts to the successive action of the fuel and gas mixture nitriding.
  • the method of the invention can include an additional processing step vacuum diffusion of the parts, after they have been subjected to the action of the fuel and gas mixture nitriding.
  • Such treatment can be carried out at a temperature from about 750 to about 1050 ° C, under pressures not exceeding 100 hPa.
  • Metallic alloys susceptible to be treated by the process of the invention can be of various types. We can in particular use cobalt-based steels and superalloys. Among steels, the process advantageously applies to treatment of passivable steels, containing by example 2 to 9% chromium and to the treatment of steels stainless steel containing for example 9 to 18% chromium, thanks to the low pressure technique. The treatment of such steels allows more enrich nitrogen to a high degree up to 4%.
  • Nitrogen can also partly enter into a solid solution in the matrix, its beneficial action in this form on the corrosion resistance already recognized.
  • the method of the invention so allows on these steels to get in the layer superficial, the C / N ratio offering the best compromise for desired strength properties wear and / or corrosion resistance, by example.
  • the method of the invention allows, by expanding the temperature range, by possibility to link in a simple way different simultaneous or alternating enrichment sequences in carbon and / or nitrogen, to realize gradients in very varied carbon and nitrogen and this on steels very diverse, even passive.
  • the subject of the invention is also steel parts obtained by this process.
  • These parts can be, for example, steel parts passivable comprising 2 to 9% chromium, which are enriched in nitrogen on their surface up to a content 2% by mass, or stainless steel parts comprising 9 to 18% chromium, which are enriched in nitrogen on their surface up to a content of 4% mass.
  • a so-called double vacuum oven can be used with hot walls or an oven with cold walls, such as the devices described in FR-A-2 663 953.
  • steps 6) and 7) can be repeated several times if necessary.
  • the pressure in the tank is preferably maintained at approximately 25 hPa.
  • a preliminary austenitization step is carried out under vacuum at 10 -2 hPa, at a temperature of 850 ° C., for 30 minutes.
  • Steps 6) and 7) are then carried out under the conditions given in table 2.
  • the reference of the alloys used, the compositions of which are given in table 1, has also been specified.
  • step 6) corresponds to carbonitriding with simultaneous shipment ethylene and ammonia and step 7) is a diffusion treatment under vacuum.
  • step 6) corresponds to carbonitriding with simultaneous shipment ethylene and ammonia (at a lower rate) and step 7) is a nitriding treatment with ammonia alone.
  • step 6) corresponds to a carburetion and step 7) to a nitriding.
  • step 6) corresponds to carbonitriding with simultaneous shipment ethylene and ammonia, but the ammonia flow is very high and step 7) is a diffusion processing under vacuum.
  • step 6 which corresponds to a carbonitriding by simultaneous shipment of ethylene and of ammonia, for a longer period than that of previous examples.
  • the process of the invention is therefore very advantageous because it leads to degrees of enrichment much higher nitrogen than we can get with the conventional methods of carbonitriding where the nitrogen content at the surface are at most about 0.3%

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Solid-Phase Diffusion Into Metallic Material Surfaces (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Ceramic Products (AREA)
  • Inorganic Fibers (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention concerns a method for carbonitriding metal alloy parts which consists in treating said parts with a fuel mixture consisting of ethylene and hydrogen and with a nitriding gas consisting of ammonia, under pressure less than 100 hPa and at a temperature of about 750 to 1050 DEG C. The invention is particularly advantageous for treating passivable and stainless steel since it enables to attain very high surface enrichment in nitrogen.

Description

Domaine techniqueTechnical area

La présente invention a pour objet un procédé de carbonitruration de pièces en alliage métallique.The subject of the present invention is a carbonitriding process of alloy parts metallic.

Elle s'applique en particulier à la carbonitruration de pièces en acier, notamment d'aciers riches en chrome utilisables dans les industries de pointe et l'industrie automobile.It applies in particular to the carbonitriding of steel parts, in particular of steel rich in chromium usable in the industries of cutting edge and the automotive industry.

Etat de la technique antérieureState of the art

La carbonitruration est un traitement thermochimique de diffusion simultanée de carbone et d'azote à partir de la surface d'un alliage ferreux à l'état solide. Elle s'effectue généralement dans un four étanche, dans lequel on maintient une atmosphère contrôlée, constituée d'un gaz support auquel on ajoute si nécessaire, pour atteindre le potentiel carbone souhaité, un gaz d'enrichissement en carbone, et en plus, un gaz azoté. Généralement, le gaz support est un gaz de générateur endothermique comprenant un alcane qui est oxydé en monoxyde de carbone CO, car on réalise l'oxydation en défaut d'air par rapport à la réaction stoechiométrique qui transformerait tout le carbone en CO2. Les gaz utilisés peuvent être des mélanges azote-méthanol ou des mélanges endothermiques à base d'hydrocarbure et d'ammoniac, comme il est décrit dans « Les Techniques de l'Ingénieur, M1226-8 à 14, juillet 1994, [1].Carbonitriding is a thermochemical treatment of simultaneous diffusion of carbon and nitrogen from the surface of a ferrous alloy in the solid state. It is generally carried out in a sealed oven, in which a controlled atmosphere is maintained, consisting of a support gas to which is added if necessary, to achieve the desired carbon potential, a carbon enrichment gas, and in addition, a nitrogen gas. Generally, the support gas is an endothermic generator gas comprising an alkane which is oxidized to carbon monoxide CO, since oxidation is carried out in the absence of air with respect to the stoichiometric reaction which would transform all the carbon into CO 2 . The gases used can be nitrogen-methanol mixtures or endothermic mixtures based on hydrocarbon and ammonia, as described in “The Engineering Techniques, M1226-8 to 14, July 1994, [1].

Ainsi, le procédé classique met en oeuvre des atmosphères qui contiennent toutes de l'oxygène dû à la présence ou à la formation de CO. L'oxygène libéré par la décomposition du CO conduit à une oxydation superficielle de l'acier qui, d'une part, freine l'absorption du carbone et, d'autre part, conduit à des structures néfastes au plan des caractéristiques mécaniques de la pièce traitée, fatigue de contact par exemple. Il faut signaler que les pièces carbonitrurées de cette façon sont le plus souvent utilisées en l'état, sans aucune retouche mécanique de la surface.Thus, the conventional method implements atmospheres that all contain oxygen the presence or formation of CO. Oxygen released by the decomposition of CO leads to oxidation surface of the steel which, on the one hand, brakes absorption of carbon and, on the other hand, leads to harmful structures in terms of characteristics mechanical of the treated part, contact fatigue by example. It should be noted that the carbonitrided parts that way are most often used in the state, without any mechanical touch-up of the surface.

Le document FR-A-2 663 953, [2] décrit un procédé et une installation de cémentation de pièces en alliage métallique à basse pression évitant la présence d'oxygène. Cette technique basse pression n'a toutefois jamais été envisagée pour réaliser des traitements de carbonitruration.The document FR-A-2 663 953, [2] describes a process and an installation for case hardening of low pressure metal alloy avoiding the presence oxygen. However, this low pressure technique never been considered for carrying out carbonitriding.

Exposé de l'inventionStatement of the invention

La présente invention a pour objet un procédé de carbonitruration qui permet d'éviter la présence néfaste d'oxygène, lors du traitement thermochimique de diffusion du carbone et de l'azote dans la pièce en alliage métallique.The subject of the present invention is a carbonitriding process which avoids the harmful presence of oxygen during treatment thermochemical diffusion of carbon and nitrogen in the metal alloy part.

Selon l'invention, le procédé de carbonitruration de pièces en alliage métallique consiste à soumettre lesdites pièces à l'action d'un mélange carburant constitué d'éthylène et d'hydrogène, et à l'action d'un gaz nitrurant constitué d'ammoniac, sous une pression inférieure à 100 hPa et à une température d'environ 750 à environ 1050°C.According to the invention, the method of carbonitriding of metal alloy parts consists in subjecting said documents to the action of a fuel mixture consisting of ethylene and hydrogen, and the action of a nitriding gas consisting of ammonia, under a pressure of less than 100 hPa and at a temperature from about 750 to about 1050 ° C.

Dans ce procédé, l'apport de carbone se fait par la dissociation directe d'un hydrocarbure, en l'occurrence l'éthylène, dans l'enceinte d'un four à vide, et l'apport d'azote provient de la dissociation du gaz ammoniac, selon la réaction activée thermiquement : 2NH3 → N2 + 3H2. In this process, the supply of carbon is made by the direct dissociation of a hydrocarbon, in this case ethylene, in the enclosure of a vacuum furnace, and the supply of nitrogen comes from the dissociation. ammonia gas, depending on the thermally activated reaction: 2NH 3 → N 2 + 3H 2 .

Selon l'invention, on utilise pour ce traitement de carbonitruration des températures plus élevées que celles utilisées habituellement pour ce type de réaction, qui se situaient généralement dans un domaine de 400 à 600°C.According to the invention, one uses for this carbonitriding temperatures treatment more higher than those usually used for this type of reaction, which were usually in a range from 400 to 600 ° C.

Aux températures plus élevées utilisées dans l'invention, la réaction de dissociation de l'ammoniac est thermodynamiquement totale, mais sa cinétique est faible. De ce fait, il existe encore au niveau de la pièce de l'ammoniac à dissocier, générant de l'azote naissant actif. C'est pour cette raison que l'on peut utiliser l'ammoniac pour l'apport d'azote.At higher temperatures used in the invention, the dissociation reaction of ammonia is thermodynamically total, but its kinetics is weak. As a result, it still exists at level of the ammonia part to be dissociated, generating active nascent nitrogen. It is for this reason that ammonia can be used for nitrogen supply.

D'autre part, le fait de travailler sous pression réduite, permet de bénéficier d'une vitesse de passage du gaz dans la charge supérieure à la cinétique de dissociation.On the other hand, the fact of working under reduced pressure, allows to benefit from a speed of passage of gas in the charge greater than the kinetics of dissociation.

La pression utilisée peut être en particulier dans la gamme de 10 à 100 hPa.The pressure used can be particularly in the range of 10 to 100 hPa.

Un des autres avantages du procédé de l'invention est de pouvoir enrichir la surface de la pièce en carbone et en azote dans un domaine de température beaucoup plus large, depuis environ 750 à environ 1050°C, selon les séquences d'enrichissement envisagées. En effet, l'utilisation de la réaction de dissociation de l'éthylène à basse pression permet de pouvoir apporter du carbone dès 750°C et donc ainsi en diminuant la température de bénéficier d'un pouvoir nitrurant plus important de l'ammoniac car la disponibilité en azote atomique utile pour la diffusion, est plus grande. Ceci permet d'accroítre les possibilités d'enrichissement superficiel en carbone et en azote.One of the other advantages of the the invention is to be able to enrich the surface of the carbon and nitrogen part in a range of much wider temperature, from around 750 to around 1050 ° C, depending on the enrichment sequences considered. Indeed, the use of the reaction of dissociation of ethylene at low pressure allows be able to provide carbon from 750 ° C and thus lowering the temperature to benefit from a power nitriding more important ammonia because the availability of atomic nitrogen useful for diffusion, is greater. This increases the possibilities for surface carbon enrichment and in nitrogen.

Ainsi selon l'invention, on peut obtenir des degrés et des profondeurs d'enrichissement en carbone et en azote voulus en choisissant de façon appropriée les débits d'éthylène et d'ammoniac, la température et la durée du traitement par le mélange carburant et le gaz nitrurant en fonction de l'alliage constituant lesdites pièces.Thus according to the invention, one can obtain enrichment degrees and depths in carbon and nitrogen desired by choosing the flow rates of ethylene and ammonia, the temperature and duration of treatment with the mixture fuel and nitriding gas depending on the alloy constituting said parts.

Selon l'invention, on peut réaliser la carbonitruration, soit en soumettant lesdites pièces à l'action simultanée du mélange carburant et du gaz nitrurant, soit en soumettant lesdites pièces à l'action successive du mélange carburant et du gaz nitrurant.According to the invention, the carbonitriding, either by subjecting said parts to the simultaneous action of the fuel and gas mixture nitriding, either by subjecting said parts to the successive action of the fuel and gas mixture nitriding.

On peut encore effectuer le traitement en soumettant les pièces à l'action simultanée du mélange carburant et du gaz nitrurant, puis en les soumettant à l'action du gaz nitrurant seul.You can still perform the treatment by subjecting the pieces to the simultaneous action of mixing fuel and nitriding gas and then submitting them to the action of nitriding gas alone.

Ces étapes peuvent être répétées et combinées entre elles en utilisant des débits, température et durées différentes, situées dans les gammes données ci-dessus.These steps can be repeated and combined with each other using flow rates, different temperature and duration, located in ranges given above.

Enfin, le procédé de l'invention peut comprendre une étape complémentaire de traitement de diffusion sous vide des pièces, après qu'elles aient été soumises à l'action du mélange carburant et du gaz nitrurant. Un tel traitement peut être effectuée à une température d'environ 750 à environ 1050°C, sous des pressions ne dépassant pas 100 hPa.Finally, the method of the invention can include an additional processing step vacuum diffusion of the parts, after they have been subjected to the action of the fuel and gas mixture nitriding. Such treatment can be carried out at a temperature from about 750 to about 1050 ° C, under pressures not exceeding 100 hPa.

Les alliages métalliques susceptibles d'être traités par le procédé de l'invention peuvent être de divers types. On peut en particulier utiliser des aciers et des superalliages à base de cobalt. Parmi les aciers, le procédé s'applique avantageusement au traitement des aciers passivables, contenant par exemple 2 à 9 % de chrome et au traitement d'aciers inoxydables contenant par exemple 9 à 18 % de chrome, grâce à la technique de la basse pression. Le traitement de tels aciers permet de plus de les enrichir en azote à un degré élevé pouvant atteindre 4 %.Metallic alloys susceptible to be treated by the process of the invention can be of various types. We can in particular use cobalt-based steels and superalloys. Among steels, the process advantageously applies to treatment of passivable steels, containing by example 2 to 9% chromium and to the treatment of steels stainless steel containing for example 9 to 18% chromium, thanks to the low pressure technique. The treatment of such steels allows more enrich nitrogen to a high degree up to 4%.

Actuellement, ces aciers inoxydables sont, pour certaines applications liées à l'usure, utilisés à l'état cémenté. Après cémentation et traitement d'emploi, la couche superficielle durcie est très riche en carbures de chrome, ce qui dégrade fortement la résistance à la corrosion de ces aciers naturellement inoxydables avant cémentation.Currently, these stainless steels are, for certain wear-related applications, used for the case hardened state. After cementation and treatment the hardened surface layer is very rich chrome carbides, which greatly degrades the corrosion resistance of these steels naturally stainless before cementation.

Le fait de pouvoir substituer en surface une partie du carbone par de l'azote, permet de former des précipités de nature différente, et ainsi de consommer moins de chrome de la matrice. L'azote peut également entrer en partie en solution solide dans la matrice, son action bénéfique sous cette forme sur la tenue à la corrosion étant déjà reconnue.Being able to substitute on the surface a part of the carbon by nitrogen, allows to form precipitates of a different nature, and so consume less chromium from the matrix. Nitrogen can also partly enter into a solid solution in the matrix, its beneficial action in this form on the corrosion resistance already recognized.

Par sa souplesse, le procédé de l'invention permet donc sur ces aciers d'obtenir dans la couche superficielle, le rapport C/N offrant le meilleur compromis pour les propriétés recherchées de résistance à l'usure et/ou de résistance à la corrosion, par exemple.By its flexibility, the method of the invention so allows on these steels to get in the layer superficial, the C / N ratio offering the best compromise for desired strength properties wear and / or corrosion resistance, by example.

En fait, le procédé de l'invention permet, par l'élargissement du domaine de température, par la possibilité d'enchaíner de façon simple différentes séquences d'enrichissement simultanées ou alternées en carbone et/ou en azote, de réaliser des gradients en carbone et azote très variés et ceci sur des aciers très divers, même passifs.In fact, the method of the invention allows, by expanding the temperature range, by possibility to link in a simple way different simultaneous or alternating enrichment sequences in carbon and / or nitrogen, to realize gradients in very varied carbon and nitrogen and this on steels very diverse, even passive.

Aussi, l'invention a également pour objet des pièces en acier obtenues par ce procédé. Ces pièces peuvent être, par exemple, des pièces en acier passivable comprenant 2 à 9 % de chrome, qui sont enrichies en azote sur leur surface jusqu'à une teneur de 2 % en masse, ou des pièces en acier inoxydable comprenant 9 à 18 % de chrome, qui sont enrichies en azote sur leur surface jusqu'à une teneur de 4 % en masse.The subject of the invention is also steel parts obtained by this process. These parts can be, for example, steel parts passivable comprising 2 to 9% chromium, which are enriched in nitrogen on their surface up to a content 2% by mass, or stainless steel parts comprising 9 to 18% chromium, which are enriched in nitrogen on their surface up to a content of 4% mass.

Pour mettre en oeuvre le procédé de l'invention, on peut utiliser un four à double vide dit à parois chaudes ou un four à parois froides, tels que les dispositifs décrits dans FR-A-2 663 953.To implement the method of the invention, a so-called double vacuum oven can be used with hot walls or an oven with cold walls, such as the devices described in FR-A-2 663 953.

A titre d'exemple, le procédé peut comprendre les étapes suivantes :

  • 1) prévidage de la cuve du four jusqu'à une pression de 10-1 hPa de façon à éliminer l'air,
  • 2) remplissage de la cuve par de l'azote à la pression atmosphérique,
  • 3) enfournement de la cuve contenant les pièces métalliques et mise sous vide de la cuve à environ 10-2 hPa,
  • 4) chauffage jusqu'à la température d'austénitisation avec des paliers si nécessaire, et maintien à cette température pendant 30 minutes pour l'homogénéisation des pièces,
  • 5) introduction d'hydrogène jusqu'à 500 hPa, de préférence ou moins selon le type de four,
  • 6) traitement de carbonitruration qui peut être effectué de différentes façons :
  • a) une période d'enrichissement en carbone par introduction du gaz carburant éthylène, suivie d'une période d'enrichissement en azote par introduction d'ammoniac, ou l'inverse, ou
  • a') période d'enrichissement en carbone et en azote par introduction simultanée d'éthylène et d'ammoniac,
  • 7) éventuellement un traitement d'enrichissement analogue à celui de l'étape 6), ou un traitement de diffusion sous vide à une température de 750 à 1050°C, sous une pression de 10-1 hPa, par exemple, et
  • 8) introduction d'azote dans le four en vue du défournement.
  • By way of example, the method can include the following steps:
  • 1) preheating of the oven tank to a pressure of 10 -1 hPa so as to eliminate the air,
  • 2) filling the tank with nitrogen at atmospheric pressure,
  • 3) charging the tank containing the metal parts and vacuuming the tank at around 10 -2 hPa,
  • 4) heating to the austenitization temperature with stages if necessary, and maintaining at this temperature for 30 minutes for the homogenization of the parts,
  • 5) introduction of hydrogen up to 500 hPa, preferably or less depending on the type of oven,
  • 6) carbonitriding treatment which can be carried out in different ways:
  • a) a carbon enrichment period by introduction of the ethylene fuel gas, followed by a nitrogen enrichment period by introduction of ammonia, or vice versa, or
  • a ') carbon and nitrogen enrichment period by simultaneous introduction of ethylene and ammonia,
  • 7) optionally an enrichment treatment similar to that of step 6), or a diffusion treatment under vacuum at a temperature of 750 to 1050 ° C., under a pressure of 10 -1 hPa, for example, and
  • 8) introduction of nitrogen into the furnace with a view to charging.
  • Il est à noter que les étapes 6) et 7) peuvent être répétées plusieurs fois si nécessaire.Note that steps 6) and 7) can be repeated several times if necessary.

    Lors de l'envoi des gaz éthylène et ammoniac, la pression dans la cuve est de préférence maintenue à environ 25 hPa.When sending ethylene gases and ammonia, the pressure in the tank is preferably maintained at approximately 25 hPa.

    Exposé détaillé des modes de réalisationDetailed description of the embodiments

    D'autres caractéristiques et avantages de l'invention ressortiront des exemples de réalisations qui suivent donnés bien entendu à titre illustratif et non limitatif.Other features and benefits of the invention will emerge from examples of embodiments which follow given of course by way of illustration and not limiting.

    Dans les exemples qui suivent on a utilisé les alliages répertoriés dans le tableau 1 dont les compositions (% en masse) sont données également dans le tableau 1.In the following examples we used the alloys listed in Table 1, the compositions (% by mass) are also given in table 1.

    Dans ces exemples, on a suivi le mode opératoire général décrit ci-dessus, pour les étapes 1 à 5 et 8 et les étapes 6 et 7 ont été réalisées en utilisant des débits d'éthylène et d'ammoniac et des séquences d'enrichissement et/ou de diffusion différentes.In these examples, we followed the mode general procedure described above, for steps 1 to 5 and 8 and steps 6 and 7 were carried out in using ethylene and ammonia flow rates and enrichment and / or dissemination sequences different.

    Dans tous les exemples, on réalise une étape préalable d'austénitisation sous vide à 10-2 hPa, à une température de 850°C, pendant 30 minutes. On effectue ensuite les étape 6) et 7) dans les conditions données dans le tableau 2. Dans ce tableau, on a spécifié également la référence des alliages utilisés dont les compositions sont données dans le tableau 1.In all the examples, a preliminary austenitization step is carried out under vacuum at 10 -2 hPa, at a temperature of 850 ° C., for 30 minutes. Steps 6) and 7) are then carried out under the conditions given in table 2. In this table, the reference of the alloys used, the compositions of which are given in table 1, has also been specified.

    Dans les exemples 1 et 2, l'étape 6) correspond à une carbonitruration avec envoi simultané d'éthylène et d'ammoniac et l'étape 7) est un traitement de diffusion sous vide.In examples 1 and 2, step 6) corresponds to carbonitriding with simultaneous shipment ethylene and ammonia and step 7) is a diffusion treatment under vacuum.

    Dans les exemples 3 et 4, l'étape 6) correspond à une carbonitruration avec envoi simultané d'éthylène et d'ammoniac ( à un débit plus faible) et l'étape 7) est un traitement de nitruration par l'ammoniac seul.In examples 3 and 4, step 6) corresponds to carbonitriding with simultaneous shipment ethylene and ammonia (at a lower rate) and step 7) is a nitriding treatment with ammonia alone.

    Dans les exemples 5 et 6, l'étape 6) correspond à une carburation et l'étape 7) à une nitruration.In examples 5 and 6, step 6) corresponds to a carburetion and step 7) to a nitriding.

    Dans les exemples 7 à 9, l'étape 6) correspond à une carbonitruration avec envoi simultané d'éthylène et d'ammoniac, mais le débit d'ammoniac est très élevé et l'étape 7) est un traitement de diffusion sous vide.In examples 7 to 9, step 6) corresponds to carbonitriding with simultaneous shipment ethylene and ammonia, but the ammonia flow is very high and step 7) is a diffusion processing under vacuum.

    Dans les exemples 10 à 16, on réalise seulement l'étape 6) qui correspond à une carbonitruration par envoi simultané d'éthylène et d'ammoniac, pendant une durée supérieure à celle des exemples précédents.In examples 10 to 16, we carry out only step 6) which corresponds to a carbonitriding by simultaneous shipment of ethylene and of ammonia, for a longer period than that of previous examples.

    Les résultats obtenus dans chaque exemple, c'est-à-dire les profils d'enrichissement superficiel en carbone et en azote (en % en masse) pour chacun des alliages traités, sont donnés dans les tableaux 3 à 8.The results obtained in each example, i.e. the surface enrichment profiles in carbon and nitrogen (in% by mass) for each of the alloys treated, are given in Tables 3 to 8.

    Les résultats obtenus dans les exemples 1 à 6 sur des nuances classiques de carbonitruration sont voisins de ceux que l'on peut obtenir en réalisant une carbonitruration gazeuse classique.The results obtained in examples 1 to 6 on conventional carbonitriding grades are neighbors of those that can be obtained by performing a conventional gaseous carbonitriding.

    Dans les exemples 7 à 9, on obtient de bons résultats en traitant des alliages plus riches en chrome, donc plus passifs.In Examples 7 to 9, good results are obtained results by processing alloys richer in chrome, therefore more passive.

    Dans les exemples 10 à 16, on observe que l'on peut atteindre superficiellement des valeurs très élevées en azote sur des aciers inoxydables riches en chrome où les taux d'azote atteignent respectivement 2,86 et 4 % d'azote dans les exemples 14 et 15. Ainsi, l'azote remplace en partie le carbone superficiel, ce qui permet d'obtenir des couches avec des propriétés particulières.In Examples 10 to 16, it is observed that we can reach very superficial values high in nitrogen on stainless steels rich in chromium where nitrogen levels reach respectively 2.86 and 4% nitrogen in Examples 14 and 15. Thus, nitrogen partially replaces surface carbon, which which allows to obtain layers with properties special.

    Le procédé de l'invention est donc très avantageux car il conduit à des degrés d'enrichissement en azote beaucoup plus élevés que ceux que l'on peut obtenir avec les procédés classiques de carbonitruration où les teneurs en azote en surface sont au plus d'environ 0,3 % The process of the invention is therefore very advantageous because it leads to degrees of enrichment much higher nitrogen than we can get with the conventional methods of carbonitriding where the nitrogen content at the surface are at most about 0.3%

    Références citéesReferences cited

  • [1] : Techniques de l'Ingénieur M 1226-8 à 14, Juillet 1994[1]: Engineering techniques M 1226-8 to 14, July 1994
  • [2] : FR-A-2 663 953[2]: FR-A-2 663 953
  • AcierSteel CVS NiOr CrCr MoMB VV Alal 20 NC 620 NC 6 0,170.17 1,601.60 0,850.85 27 CD 427 CD 4 0,270.27 1,01.0 0,20.2 20 CD 1220 CD 12 0,250.25 3,03.0 0,40.4 32 CDV 1332 CDV 13 0,300.30 3,03.0 1,01.0 0,200.20 40 CAD 6.1240 CAD 6.12 0,400.40 1,81.8 0,250.25 1,01.0 20 DN 34.1320 DN 34.13 0,200.20 3,03.0 3,53.5 Z 15 CN 17.03Z 15 CN 17.03 0,160.16 2,02.0 17,017.0 Z 12 CNDV 12Z 12 CNDV 12 0,120.12 2,52.5 11,511.5 1,61.6 0,300.30 ExEx AcierSteel Etape 6)Step 6) Etape 7)Step 7) t
    (°C)
    t
    (° C)
    durée
    (min)
    duration
    (Min)
    C2H4
    (l/h)
    C 2 H 4
    (L / h)
    NH3
    (l/h)
    NH 3
    (L / h)
    P
    (hPa)
    P
    (HPa)
    t
    (°C)
    t
    (° C)
    durée
    (min)
    duration
    (Min)
    NH3
    (l/n)
    NH 3
    (L / n)
    P
    (hPa)
    P
    (HPa)
    11 20NC620NC6 850850 4545 5050 300300 2525 850850 4545 -- 0,10.1 22 27CD427CD4 33 20NC620NC6 850850 4545 5050 100100 2525 850850 4545 100100 2525 44 27CD427CD4 55 20NC620NC6 850850 4545 5050 -- 2525 850850 4545 100100 2525 66 27CD427CD4 77 27CD427CD4 88 32CVD1332CVD13 850850 4545 5050 600600 2525 850850 4545 -- 0,10.1 99 Z15CN17.03Z15CN17.03 1010 20NC620NC6 1111 27D427D4 1212 20CD1220CD12 1313 40CAD6.1240CAD6.12 850850 360360 5050 300300 2525 1414 Z12CNDV12Z12CNDV12 1515 Z15CN17.03Z15CN17.03 1616 20DN34.1320DN34.13
    ExEx 11 22 AlliageAlloy 20 NC 620 NC 6 27 CD 427 CD 4 Profondeur
    (mm)
    Depth
    (Mm)
    C %VS % N %NOT % C %VS % N %NOT %
    0,050.05 0,500.50 0,3040.304 0,610.61 0,3240.324 0,150.15 0,450.45 0,2150.215 0,580.58 0,2230.223 0,250.25 0,450.45 0,1130.113 0,510.51 0,1220.122 0,350.35 0,330.33 0,0390,039 0,470.47 0,0430.043 coeurheart 0,190.19 0,00590.0059 0,270.27 0,00800.0080
    ExEx 33 44 AlliageAlloy 20 NC 620 NC 6 27 CD 427 CD 4 Profondeur
    (mm)
    Depth
    (Mm)
    C %VS % N %NOT % C %VS % N %NOT %
    0,050.05 0,720.72 0,2970.297 0,750.75 0,2790.279 0,150.15 0,660.66 0,2030.203 0,690.69 0,1890.189 0,250.25 0,570.57 0,1140.114 0,610.61 0,1020,102 0,350.35 0,460.46 0,0490.049 0,510.51 0,0370,037 coeurheart 0,190.19 0,00590.0059 0,270.27 0,00810.0081
    ExEx 55 66 AlliageAlloy 20 NC 620 NC 6 27 CD 427 CD 4 Profondeur
    (mm)
    Depth
    (Mm)
    C %VS % N %NOT % C %VS % N %NOT %
    0,050.05 0,790.79 0,1480,148 0,820.82 0,1650,165 0,150.15 0,710.71 0,0940.094 0,720.72 0,0780.078 0,250.25 0,560.56 0,0290,029 0,570.57 0,0280,028 0,350.35 0,370.37 0,00920.0092 0,440.44 0,0120.012 coeurheart 0,190.19 0,00590.0059 0,270.27 0,00810.0081
    ExEx 77 88 99 AlliageAlloy 27 CD427 CD4 32CDV1332CDV13 Z15CN17.03Z15CN17.03 Profondeur
    (mm)
    Depth
    (Mm)
    C %VS % N %NOT % C %VS % N %NOT % C %VS % N %NOT %
    0,050.05 0,630.63 0,220.22 0,340.34 0,730.73 0,890.89 2,002.00 0,150.15 0,580.58 0,190.19 0,600.60 0,290.29 0,770.77 0,080.08 0,250.25 0,540.54 0,120.12 0,550.55 0,030.03 0,330.33 0,050.05 0,350.35 0,460.46 0,050.05 0,440.44 0,010.01 0,200.20 0,050.05
    ExEx 1010 1111 1212 1313 AlliageAlloy 20NC620NC6 27CD427CD4 20CD1220CD12 40CAD6.1240CAD6.12 Profondeur
    (mm)
    Depth
    (Mm)
    C %VS % N %NOT % C %VS % N %NOT % C %VS % N %NOT % C %VS % N %NOT %
    0,050.05 0,980.98 0,520.52 0,930.93 0,440.44 0,600.60 0,890.89 0,810.81 0,980.98 0,150.15 0,860.86 0,510.51 0,860.86 0,440.44 0,540.54 0,800.80 0,770.77 0,840.84 0,250.25 0,810.81 0,450.45 0,790.79 0,410.41 0,540.54 0,550.55 0,890.89 0,480.48 0,350.35 0,730.73 0,310.31 0,770.77 0,310.31 0,730.73 0,120.12 0,800.80 0,040.04 0,450.45 0,650.65 0,200.20 0,660.66 0,240.24 0,570.57 0,040.04 0,660.66 0,010.01 0,550.55 0,560.56 0,090.09 0,510.51 0,150.15 0,460.46 0,020.02 0,570.57 0,010.01
    ExEx 1414 1515 1616 AlliageAlloy Z12CNDV12Z12CNDV12 Z15CN17.03Z15CN17.03 20DN34.1320DN34.13 Profondeur
    (mm)
    Depth
    (Mm)
    C %VS % N %NOT % C %VS % N %NOT % C %VS % N %NOT %
    0,050.05 0,410.41 2,862.86 0,610.61 4,004.00 0,570.57 0,530.53 0,150.15 2,072.07 0,260.26 2,452.45 0,360.36 0,530.53 0,410.41 0,250.25 1,321.32 0,070.07 1,211.21 0,080.08 0,500.50 0,310.31 0,350.35 1,621.62 0,040.04 0,510.51 0,050.05 0,460.46 0,190.19 0,450.45 0,220.22 0,030.03 0,260.26 0,040.04 0,400.40 0,110.11 0,550.55 0,140.14 0,030.03 0,200.20 0,040.04 0,350.35 0,080.08

    Claims (12)

    1. Method of carbonitriding metal alloy components, in which said components are subjected to the action of a fuel mixture made up of ethylene and hydrogen and to the action of a nitriding gas consisting of ammonia, at a pressure of less than 100 hPa and at a temperature of from about 750 to 1050°C.
    2. Method according to claim 1, in which the pressure is from 10 to 100 hPa.
    3. Method according to any one of claims 1 and 2, in which the metal alloy is a steel.
    4. Method according to claim 3, in which the flow rates of ethylene and ammonia, the temperature and the duration of the treatment by the fuel mixture and the nitriding gas are chosen in such a way that nitrogen enrichment ranging up to 4 wt.%, of the surface of the component is obtained.
    5. Method according to any one of claims 1 to 4, in which the metal alloy is a steel that can be passivated and which comprises 2 to 9 wt.% chromium.
    6. Method according to any one of claims 1 to 4, in which the metal alloy is a stainless steel that comprises 9 to 18 wt.% chromium.
    7. Method according to any one of claims 1 to 6, in which said components are subjected to the simultaneous action of the fuel mixture and the nitriding gas.
    8. Method according to any one of claims 1 to 6, in which said components are subjected successively to the action of the fuel mixture and the nitriding gas.
    9. Method according to any one of claims 1 to 6, in which the components are subjected 1) to the simultaneous action of the fuel mixture and the nitriding gas and then 2) to the action of the nitriding gas alone.
    10. Method according to any one of claims 1 to 9, in which, after having subjected the components to the action of the fuel mixture and the nitriding gas, the components are subjected to a diffusion treatment under vacuum at a temperature of from about 750 to 1050°C.
    11. Method according to claim 5, in which the surface of said component is enriched in nitrogen up to a content of 2 wt.%.
    12. Method according to claim 6, in which the surface of said component is enriched in nitrogen up to a content of 4 wt.%.
    EP99915850A 1998-04-28 1999-04-27 Low pressure carbonitriding method for metal alloy parts Expired - Lifetime EP1080243B1 (en)

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    FR9805311 1998-04-28
    FR9805311A FR2777911B1 (en) 1998-04-28 1998-04-28 LOW PRESSURE CARBONITRURATION OF METAL ALLOY PARTS
    PCT/FR1999/000998 WO1999055928A1 (en) 1998-04-28 1999-04-27 Low pressure carbonitriding method for metal alloy parts

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    Cited By (3)

    * Cited by examiner, † Cited by third party
    Publication number Priority date Publication date Assignee Title
    US8303731B2 (en) 2005-04-19 2012-11-06 Ecm Technologies Low pressure carbonitriding method and device
    CN103946411A (en) * 2011-10-31 2014-07-23 标致·雪铁龙汽车公司 Method for low-pressure carbonitriding having an extended temperature range in an initial nitridation phase
    US9212416B2 (en) 2009-08-07 2015-12-15 Swagelok Company Low temperature carburization under soft vacuum

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    DE50007480D1 (en) * 2000-05-24 2004-09-23 Ipsen Int Gmbh Method and device for the heat treatment of metallic workpieces
    DE10118494C2 (en) * 2001-04-04 2003-12-11 Aichelin Gesmbh Moedling Process for low pressure carbonitriding of steel parts
    AU2002221138A1 (en) * 2001-12-13 2003-06-23 Koyo Thermo Systems Co., Ltd. Vacuum carbo-nitriding method
    DE102004058838B4 (en) * 2004-12-06 2007-11-29 Schramm, Armin Nozzle insert made of steel
    DE112010005929A5 (en) * 2010-10-11 2014-01-02 Ipsen International Gmbh Method and device for carburizing and carbonitriding metallic materials
    FR2981948B1 (en) * 2011-10-31 2014-01-03 Peugeot Citroen Automobiles Sa LOW PRESSURE CARBONITRURATION PROCESS WITH REDUCED GRADIENT TEMPERATURE IN AN INITIAL NITRIDATION PHASE
    DK2804965T3 (en) 2012-01-20 2020-12-14 Swagelok Co Simultaneous flow of activating gas at low temperature carburization
    JP7450557B2 (en) * 2018-06-11 2024-03-15 スウェージロック カンパニー Chemical activation of self-passivating metals

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    CA692161A (en) * 1964-08-11 N. Ipsen Harold Method of heat treating metal parts
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    FR2271295A1 (en) * 1973-12-21 1975-12-12 Air Liquide Gas mixtures for heat treating steel - esp. for controlled carburisation
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    Cited By (6)

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    Publication number Priority date Publication date Assignee Title
    US8303731B2 (en) 2005-04-19 2012-11-06 Ecm Technologies Low pressure carbonitriding method and device
    US8784575B2 (en) 2005-04-19 2014-07-22 Ecm Technologies Low pressure carbonitriding method and device
    EP1885904B2 (en) 2005-04-19 2017-02-01 Ecm Technologies Low pressure carbonitriding method
    US9212416B2 (en) 2009-08-07 2015-12-15 Swagelok Company Low temperature carburization under soft vacuum
    CN103946411A (en) * 2011-10-31 2014-07-23 标致·雪铁龙汽车公司 Method for low-pressure carbonitriding having an extended temperature range in an initial nitridation phase
    CN103946411B (en) * 2011-10-31 2016-01-20 标致·雪铁龙汽车公司 Low pressure carbo-nitriding method on the initial nitriding stage in the temperature range of expansion

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