EP3230487A1

EP3230487A1 - Low pressure carbonitriding method and furnace

Info

Publication number: EP3230487A1
Application number: EP15817994.5A
Authority: EP
Inventors: Yves Giraud; Hubert MULIN
Original assignee: ECM Technologies SAS
Current assignee: ECM Technologies SAS
Priority date: 2014-12-11
Filing date: 2015-12-10
Publication date: 2017-10-18
Anticipated expiration: 2035-12-10
Also published as: US20170356077A1; JP2018505301A; JP7177592B2; KR20170093855A; CA2970247C; MX2017007484A; CN107406960A; KR102576343B1; WO2016092219A1; FR3029938B1; US11242594B2; FR3029938A1; CN107406960B; EP3230487B1; CA2970247A1

Abstract

The invention relates to a method for carbonitriding of a steel part arranged in a chamber, comprising first steps and second steps, a carburizing gas being injected into the chamber during the first steps only and a nitriding gas being injected into the chamber during the second steps only, at least one of the second steps being situated between two first steps, the pressure in the chamber during at least one part of said two first steps being maintained at a first value and the pressure in the chamber during at least one part of said second step situated between said two first steps being at a second value that is strictly greater than the first value.

Description

LOW PRESSURE CARBONITRUTING PROCESS AND FURNACE

The present patent application claims the priority of the French patent application FR14 / 62260 which will be considered as an integral part of the present description.

Field

The present invention relates to processes for treating steel parts, and more particularly to carbonitriding processes, that is to say introducing carbon and nitrogen at the surface of steel parts to improve its performance. hardness and fatigue resistance.

Presentation of the prior art

There are several types of processes carbonitrile ^¬ truration steel parts to one introducing carbon and nitrogen in the surface level of the parts to depths of up to several hundred micrometers.

A first category of carbonitriding processes corresponds to so-called high-pressure carbonitriding processes insofar as the enclosure containing the workpieces is maintained at a pressure generally close to atmospheric pressure for the duration of the treatment. Such a process consists, for example, in maintaining the parts at a temperature plateau, for example at approximately 880 ° C., while supplying the enclosure with a gaseous mixture consisting of methanol and ammonia. The carbonitriding step is followed by a quenching step, for example an oil quenching, and optionally a hardening step of the treated parts.

A second category of carbonitriding processes corresponds to so-called low pressure or reduced pressure carbonitriding processes, insofar as the enclosure containing the workpieces is maintained at a pressure generally less than a few hundred pascals (a few millibars).

US Pat. No. 8,303,731 describes an example of a low-pressure carbonitriding process comprising an alternation of carburizing steps and nitriding steps. Although this method gives satisfactory results, it may be desirable for certain applications to further increase the surface nitrogen enrichment of the treated pieces.

summary

An object of an embodiment is to overcome all or part of the disadvantages of low pressure carbonitriding processes and low pressure carbonitriding furnaces previously described.

Another object of an embodiment is to obtain, precisely and reproducibly, the desired carbon and nitrogen concentration profiles in the treated parts.

Another object of an embodiment is that the implementation of the carbonitriding process is compatible with the treatment of steel parts in an industrial context.

Another object of the present invention is that the low pressure carbonitriding furnace has a simple structure.

Thus, an embodiment provides a method of carbonitriding a steel part disposed in an enclosure, comprising first stages and second stages, a cementation gas being injected into the chamber only during the first stages and a gas of nitriding being injected into the chamber only during the second stages, at least one of the second stages being situated between two of the first stages, the pressure in the chamber during at least a portion of said two first steps being maintained at a first value and the pressure in the chamber during at least a portion of said second step located between said first two steps being at a second value strictly greater than the first value.

According to one embodiment, the first value is between 0.1 hPa and 20 hPa, preferably between 0.1 hPa and 10 hPa.

According to one embodiment, the second value is between 10 hPa and 250 hPa, preferably between 30 hPa and 150 hPa.

According to one embodiment, the carburizing gas is propane or acetylene.

According to one embodiment, the nitriding gas is ammonia.

According to one embodiment, the method further comprises third steps, each third step being located between two of the first steps, between two of the second steps or between one of the first steps and one of the second steps, a neutral gas being injected into the chamber during each third step.

According to one embodiment, the method further comprises first, second and third successive phases, the first phase comprising only first steps alternating with third steps, the second phase comprising the successive repetition of a cycle successively comprising a second step, a third step, a first step and a second step, and the third step comprising only second alternate steps with third steps.

According to one embodiment, at least one of the third steps directly precedes one of the second steps and the pressure is increased from the first value to the second value during said first step before the beginning of said third step.

According to one embodiment, at least one of the third steps directly precedes one of the second steps and the pressure is maintained at the first value until the end of said first step and is increased from the first value to the second value after the beginning of said third step.

According to one embodiment, the part is maintained at a temperature step.

According to one embodiment, the temperature plateau is between 800 ° C and 1050 ° C.

According to one embodiment, the temperature plateau is greater than 900 ° C.

One embodiment also provides a carbonitriding furnace for receiving a steel part, comprising gas introduction and gas extraction circuits, and a control module adapted to control the gas introduction and gas introduction circuits. extraction of gas to introduce, during the first steps and second steps, a carburizing gas into the chamber only during the first stages and a nitriding gas into the chamber only during the second stages, at least one second steps being located between two first steps, and adapted to maintain the pressure in the chamber during at least a portion of the first two steps at a first value and the pressure in the chamber during at least a portion of said second step located between the first two steps to a second value strictly greater than the first value.

According to one embodiment, the furnace further comprises a heating element and the control module is adapted to control the heating element to maintain the room at a temperature step.

Brief description of the drawings

These and other features and advantages will be set forth in detail in the following description of particular embodiments in a non-limiting manner with reference to the accompanying drawings in which:

Figure 1 schematically shows an embodiment of a low pressure carbonitriding furnace; Figure 2 illustrates an embodiment of a low pressure carbonitriding process;

FIGS. 3 to 6 illustrate more detailed embodiments of the evolution of the pressure in the carbonitriding furnace during the implementation of the embodiment of the carbonitriding process illustrated in FIG. 1 between a nitriding step and steps broadcasting; and

FIGS. 7 and 8 respectively represent carbon and nitrogen concentration profiles obtained by the implementation of a carbonitriding process according to the embodiment illustrated in FIG. 1 and a known carbonitriding process.

detailed description

The same elements have been designated with the same references in the various figures and, moreover, the various figures are not drawn to scale. For the sake of clarity, only the elements that are useful for understanding the described embodiments have been shown and are detailed.

In the following description, unless otherwise stated, the terms "approximately", "substantially", and "of the order of" mean within 10%, preferably within 5%. In addition, alternating steps A and B means a succession of steps A and B in which each step B, with the exception of the last step of the succession, is located between two steps A and each step A , with the exception of the initial stage of succession, is located between two stages B.

According to one embodiment, an alternation of carbon enrichment steps is performed in an enclosure, containing steel parts to be treated maintained at a substantially constant temperature, at least during part of the carbonitriding process. , also known as cementation steps, during which a cementation gas is injected into the chamber maintained at a first reduced pressure, and nitrogen enrichment stages, also called nitriding steps, during which a nitriding gas is injected in the chamber maintained at a second pressure greater than the first pressure. During each step of carburizing, there is no injection of nitriding gas into the chamber and during each nitriding step, there is no injection of carburizing gas into the chamber.

This advantageously makes it possible to control, in a precise and reproducible manner, the carbon and nitrogen concentration profiles obtained in the treated parts since the injection of the nitriding gas is carried out separately from the injection of the carburizing gas. In addition, since the injection of the nitriding gas is carried out in the chamber while the chamber is maintained at a pressure higher than the pressure prevailing in the chamber during the injection of the carburising gas, the enrichment in nitrogen of the treated parts is increased compared to a process in which the same pressure is maintained in the chamber during the injection of the carburizing gas and the injection of the nitriding gas.

It can be provided, between at least one carburizing step and the next nitriding step, a diffusion step during which the injection of the carburising gas and the injection of the nitriding gas into the chamber are interrupted. Likewise, there can be provided, between at least one nitriding step and the subsequent carburizing step, a diffusion step during which the injection of the carburizing gas and the injection of the nitriding gas into the chamber are interrupted. .

FIG. 1 schematically represents an embodiment of a low-pressure carbonitriding furnace 10. The furnace 10 comprises a sealed wall 12 delimiting an internal enclosure 14 in which a charge to be treated 16 is disposed, generally a large number of parts arranged on a suitable support. A vacuum at a pressure of a few hectopascals (a few millibars) to a few hundred hectopascals (a few hundred millibars) can be maintained in the chamber 14 through an extraction pipe 18 is connected to a vacuum pump 20. An in ector 22 makes it possible to introduce gases distributed in the chamber 14. By way of example, gas inlets 22, 24, 26, 28 are respectively monitored. by valves 30, 32, 34, 36. A heating element 38 is disposed in the chamber 14. A control module 40 is connected to the valves 30, 32, 34, 36 and the vacuum pump 20, and optionally to the heating element 38. The control module 40 is adapted to control the closing and opening of each valve 30, 32, 34, 36. A pressure sensor 42 and a temperature sensor 44 may be provided in FIG. 14 and connected to the control module 40. From the signal provided by the temperature sensor 44, the control module 40 is adapted to control the heating element 38 to maintain the temperature in the chamber 14 to a value substantially constant. From the signal provided by the pressure sensor 42, the control module 40 is adapted to control the suction power of the vacuum pump 20 to maintain the pressure in the chamber 14 to a set value. The control module 40 may comprise a microprocessor or a microcontroller. The control module 40 may, in whole or in part, correspond to a dedicated circuit or include a processor adapted to execute instructions of a computer program stored in a memory.

FIG. 2 represents a curve <¾ _ΘΠ1 of temperature evolution and a curve Cp _res of evolution of the pressure in the chamber 14 of the carbonitriding furnace 10 of FIG. 1 during a carbonitriding cycle according to a embodiment of the carbonitriding process.

The method comprises an initial step H corresponding to an increase of the temperature in the chamber 14 containing the charge 16 to a temperature plateau 52 which, in the present example, can correspond to a temperature of between approximately 800 ° C. and about 1050 ° C, preferably between about 880 ° C and about 960 ° C, for example of the order of 930 ° C. Step H is followed by a step PH equalizing the temperature of the parts constituting the load 16 at the temperature step 52. The steps H and PH can be carried out in the presence of a neutral gas, to which a reducing gas is optionally added. The neutral gas is, for example, nitrogen (¾). The reducing gas, for example hydrogen (¾), may be added in a proportion ranging from 1% to 5% by volume of the neutral gas. For reasons of safety, it may be desirable to limit the proportion of hydrogen to less than about 5% to prevent any risk of explosion in case the hydrogen accidentally comes into contact with the ambient atmosphere. Step PH is followed by a succession of three phases PI, PII and PIII. The phases PI, PII and PIII are carried out by maintaining the temperature in the chamber 14 at the temperature plateau 52. A quenching step Q of the load 10, for example a gas quenching, closes the carbonitriding cycle by a decrease in temperature. of the temperature. The PI phase may not be present. Similarly, phase PIII may not be present.

The PI phase comprises an alternation of carbon enrichment steps C _j , during which a cementation gas is injected into the chamber 14, and carbon diffusion stages D _j during which the carburizing gas is more injected into the enclosure 14. Preferably, the PI phase comprises at least successively a carburizing step, a diffusion step, a carburizing step and a diffusion step. By way of example, in FIG. 2, the phase PI comprises an alternation of two carburizing steps C _j and two diffusion stages D _j . The carburizing gas is, for example, propane (C3H8) or acetylene (C2¾). It can also be any other hydrocarbon (ΟχΗγ) likely to dissociate at the temperatures of the enclosure to cementer the surface of the parts to be treated.

The phase PII comprises alternating stages of enrichment in nitrogen JJ, during which a nitriding gas is injected into the chamber 14, and carbon enrichment stages CJJ during which the gas of cementation is injected into the chamber 14. During the nitriding steps NJ J, the carburising gas is not injected into the chamber 14 and, during the carburizing steps CJ J, the nitriding gas is not injected in the enclosure 14. According to one embodiment, a nitriding step JJ is followed directly by a carburizing step CJ J. According to one embodiment, a carburizing step CJ J, with the exception of the last step of CJ J cementation of the PII phase, is followed directly by a nitriding step JJ.

According to one embodiment, a diffusion step DJ J can be provided between each nitriding step J J and the cementation step CJ J following. According to one embodiment, a diffusion step DJ J may be provided between each cementation step CJ J and the cementation step CJ J nitriding J J following. Preferably, the PII phase comprises at least successively a nitriding step, a diffusion step, a cementation step and a diffusion step. By way of example, in FIG. 2, the phase PII comprises two successive cycles each comprising a nitriding step JJ, a diffusion step DJ J, a cementation step CJ J and a diffusion step DJ J. The nitriding gas is for example ammonia (NH3).

The phase PIII comprises alternating stages of enrichment in nitrogen JJJ, during which the nitriding gas is injected into the chamber 14, and stages of carbon diffusion DJ JJ during which the nitriding gas is no longer The phase PIII preferably comprises at least one nitriding step, a diffusion step, a nitriding step and a diffusion step. By way of example, in FIG. 2, the phase PIII comprises an alternation of two nitriding steps and two DJ J J diffusion stages.

By resuming the diagram of FIG. 1, a hydrocarbon (ΟχΗγ), on the inlet 24 of the valve 32 of the nitrogen, can be delivered to the inlet 22 of the valve 30 on the inlet 36 of the valve 34 of the hydrogen and the inlet 28 of the valve 36 of ammonia.

The pressure is maintained at a set point in the chamber 14 by the vacuum pump 20 controlled by the control module 40. According to one embodiment, during at least some of the cementation steps C and CJJ, the pressure in the The enclosure is, at least on some of these steps, kept substantially constant at a first value. According to one embodiment, the first pressure value is between 0.1 hPa and 20 hPa, preferably between 0.1 hPa and 10 hPa. Preferably, the pressure in the chamber 14 is kept substantially constant at the first value during at least a portion of each cementation step C _j of the first phase P1. Preferably, the pressure in the enclosure 14 is kept substantially constant at the first value during at least a portion of each cementation step CJJ of the second phase PII.

According to one embodiment, during at least some of the nitriding steps NJ and JJJ, the pressure in the chamber is maintained, at least over part of this step, substantially constant at a second value, strictly greater than the first value. . According to one embodiment, the second pressure value is between 10 hPa and 250 hPa, preferably between 30 hPa and 150 hPa. Preferably, the pressure in the chamber 14 is kept substantially constant at the second value during each nitriding step J of the third phase PIII. Preferably, the pressure in the chamber 14 is kept substantially constant at the second value during at least a portion of each NJ J nitriding step of the third PII phase.

The carbonitriding process remains a low pressure, or reduced pressure, carbonitriding process insofar as the pressure in the enclosure 14 is less than 500 mbar (500 hPa) during the entire process. According to one embodiment, the pressure in the chamber 14 is, in addition, kept substantially constant at the first value during at least a portion of each diffusion step D _j of the first phase PI, during at least a portion of each DJ J broadcast stage of the second phase PII and / or during at least a portion of each OJJJ diffusion step of the third phase PIII. According to one embodiment, the pressure in the chamber 14 is furthermore kept substantially constant at the first value during the steps H and PH. A neutral gas, for example nitrogen (¾), may, in addition, be injected during the steps H and PH and during the carburizing steps C, CJJ, nitriding NJ J, NJ JJ and diffusion D _j , DJ J Yes- Alternatively, the inert gas may be injected only during the diffusion steps D _j, DJ J, DJ and JJ not be injected during steps C carburizing and nitriding steps of Naked, Nm .

The passage of the pressure in the chamber 14 from the first value to the second value, which is strictly greater than the first value, can be obtained by temporarily reducing or stopping the suction of the vacuum pump 20. increasing the pressure in the chamber 14 from the first value to the second value can be achieved in less than 2 minutes, preferably in less than 1 minute.

The passage of the pressure in the chamber 14 of the second value to the first value, strictly less than the second value, can be obtained by temporarily increasing the suction of the vacuum pump 20, to reduce the pressure in the enclosure 14, then reducing the suction power of the vacuum pump 20 to a level adapted to maintain the pressure in the chamber 14 to the second value. Preferably, the decrease in the pressure in the chamber 14 from the second value to the first value can be achieved in less than 2 minutes, preferably in less than 1 minute.

According to one embodiment, all the gases injected into the enclosure 14 of the furnace 10 or some of them may be In such a variant, for example, during the steps of temperature rise H and of equalization of temperature PH, it is possible to inject directly into the chamber 14 a mixture of nitrogen and hydrogen. hydrogen of the type containing a proportion of hydrogen less than 5% by volume, such a proportion of hydrogen excluding any risk of explosion.

Figures 3 to 6 show curves of _C] _, C2, C3, C4 of evolution of the pressure in the chamber 14 and illustrate different configurations for varying the pressure during the succession of a first diffusion step Dl , which may correspond to a step DJ J or a step D described above, of a nitriding step N, which may correspond to a step NJ J or a step JJJ described above, and a second diffusion step D2. In the nitriding step N, nitriding gas is injected into the chamber 14. During each diffusion step D1 and D2, neutral gas is injected into the chamber 14. The injection of neutral gas into the chamber 14 can also be carried out during the nitriding step N. The variation of the pressure is carried out by modifying the suction power of the vacuum pump 20. Each curve C _] , ¾ '¾ and C4 comprises a first pressure bearing LP1 substantially constant at the first value in each diffusion step D1 and D2, a second pressure bearing LP2 substantially constant at the second value in the nitriding step N, an ascending phase PUP between the LP1 bearing and the bearing PP2 and a downward phase PDOWN between the bearing LP2 and the bearing LP1.

In the embodiment illustrated in FIG. 3, the ascending phase PUP is carried out in the nitriding step N and the downward phase PDOWN is carried out in the diffusion step D2. In the embodiment illustrated in FIG. 4, the ascending phase PUP is carried out in the nitriding step N and the downward phase PDOWN is carried out in the nitriding step N. In the embodiment illustrated in FIG. 5, the phase ascending PUP is performed in the diffusion step Dl and the PDOW down-phase is carried out in the nitriding step N. In the embodiment illustrated in FIG. 6, the ascending phase PUP is carried out in the diffusion step D1 and the down-phase PDOWN is carried out in the step of D2 broadcast. The nitriding step N is then advantageously carried out at a substantially constant pressure.

FIG. 7 represents an example of a PQ profile of weight concentration of the carbon element and an example of a PJJ profile of concentration by weight of the nitrogen element that has diffused into a treated part as a function of the depth, measured from the surface of the part during the implementation of a first carbonitriding process in which the pressure in the chamber 14 remains substantially constant at low pressure.

FIG. 8 represents an exemplary profile PQ 'of concentration by weight of the carbon element and an example of a PN' profile of concentration by weight of the nitrogen element having diffused into a treated part as a function of the depth, measured from of the surface of the part during the implementation of a second carbonitriding method according to the embodiment described above in connection with Figure 2 in which the pressure is increased during the nitriding steps.

For the first and second methods of carboni ^¬ truration, the carburizing gas was acetylene, nitriding gas was ammonia and the inert gas was nitrogen. In the first and second carbonitriding processes, the carbonitriding was carried out at a temperature level of 920 ° C. The quenching step Q was gas quenching.

The first and second carbonitriding processes included the following steps:

steps H and PH: 70 minutes in full;

PI phase: alternation of four carburizing stages C _j (128 s, 60 s, 56 s and 55 s respectively) and four diffusion stages D _j (185 s, 302 s, 420 s and 60 s respectively); PII phase: alternation of three NJJ nitriding steps (respectively 394 s, 424 s and 402 s), six DJJ diffusion steps (93 s, 120 s, 130 s, 180 ° s, 227 ° s and 120 s respectively). s) and three CJJ cementation steps (54 s each); and

phase PIII: alternation of three nitriding stages ^N III (of 300 s each) and three diffusion stages DJJJ (respectively of 120 s, 120 s and 862 s).

The pressure in the chamber 14 was kept substantially at 8 mbar (8 hPa) during all stages H, PH, C _j, D _j, YJCs DJJ and DJJJ and the pressure in the chamber 14 was maintained at substantially 45 mbar (45 hPa) during the NJJ and NJJJ steps except for the first stage NJJ which was carried out at the pressure of 8 mbar (8 hPa).

The inventors have demonstrated that increasing the pressure during at least some NJJ and / or NJJJ nitriding steps makes it possible to obtain an increase in the nitrogen enrichment of the treated parts. In particular, for the first method, the nitrogen concentration was 0.1% by weight to 25 μm, 0.09% by weight to 100 μm, 0.045% by weight to 200 μm and 0.025% by weight. weight at 300 μm. For the second method, the nitrogen concentration was 0.4 wt% at 25 μm, 0.29 wt% at 100 μm, 0.14 wt% at 200 μm and 0.06 wt% at 300 μm.

The inventors have shown that increasing the pressure during at least some NJJ and / or NJJJ nitriding steps makes it possible, moreover, to obtain an increase in the carbon enrichment of the treated parts. In particular, for the first method, the carbon concentration was 0.725% by weight to 50 μm, 0.71% by weight to 100 μm, 0.675% by weight to 200 μm, and 0.6% by weight to 100 μm. 300 μm. For the second method, the carbon concentration was 0.8 wt% to 50 um, 0.8 wt% to 100 um, 0.775 wt% to 200 um and 0.68 wt% to 300 um. According to a variant of the invention, the nitriding gas can be injected during step H of temperature rise, as soon as the temperature in the chamber 14 exceeds a given temperature, and / or during the equalizing step PH in temperature. By way of example, when the nitriding gas is ammonia, the injection can be performed as soon as the temperature in the enclosure 14 exceeds about 800 ° C.

The fact that the carburizing and nitriding gases are not injected simultaneously makes it possible to increase the pressure in the chamber 14 during at least some of the nitriding steps NJ and / or NJJ J. This results in a better nitrogen enrichment. and carbon treated parts.

In addition, the fact that carburizing and nitriding gases are not injected simultaneously makes it possible to obtain the desired carbon and nitrogen concentration profiles accurately and reproducibly. Indeed, if the nitriding gas is injected simultaneously with the carburizing gas, there is a dilution of the carburizing gas and the nitriding gas. This is not a factor favoring the reaction of carbon from the carburising gas or the reaction of the nitrogen from the nitriding gas with the parts to be treated, which slows the enrichment of the parts in nitrogen and carbon. In addition, if the carburizing gas and the nitriding gas are mixed, the control of the gaseous environment in the chamber 14 can hardly be carried out accurately, which makes it more difficult to obtain accurately and reproducibly, desired nitrogen and carbon concentration profiles of the treated pieces.

Of course, the present invention is susceptible of various variations and modifications which will be apparent to those skilled in the art. For example, the previously described gas quenching step can be replaced by an oil quenching step.

Claims

1. A method of carbonitriding a piece (16) of steel disposed in a chamber (14), comprising first steps and second stages, a carburizing gas being injected into the chamber only during the first stages and a gas of nitriding being injected into the chamber only during the second stages, at least one of the second stages being situated between two of the first stages, the pressure in the chamber during at least a portion of said first two stages being maintained at a first value and the pressure in the enclosure during at least a portion of said second stage located between said first two steps being at a second value strictly greater than the first value.

2. The method of claim 1, wherein the first value is between 0.1 hPa and 20 hPa, preferably between 0.1 hPa and 10 hPa.

3. The method of claim 1 or 2, wherein the second value is between 10 hPa and 250 hPa, preferably between 30 hPa and 150 hPa.

The process of any one of claims 1 to 3, wherein the carburizing gas is propane or

Acetylene.

5. Process according to any one of claims 1 to 4, wherein the nitriding gas is ammonia.

The method of any one of claims 1 to 5, further comprising third steps, each third step being located between two of the first steps, between two of the second steps or between one of the first steps and the first step. one of the second stages, a neutral gas being injected into the chamber during each third stage.

The method according to claim 6, comprising first, second and third successive phases, and wherein the first phase comprises only first steps alternated with third steps, wherein the second phase comprises the successive repetition of a cycle comprising successively a second step, a third step, a first step and a second step, and wherein the third phase comprises only second steps alternated with third steps.

The method of claim 6 or 7, wherein at least one of the third steps directly precedes one of the second steps and wherein the pressure is increased from the first value to the second value during said first step before the beginning. of said third step.

The method of claim 6 or 7, wherein at least one of the third steps directly precedes one of the second steps and wherein the pressure is held at the first value until the end of said first step and is increased from the first value to the second value after the beginning of said third step.

10. A method according to any one of claims 1 to 9, wherein the part (6) is maintained at a temperature step.

11. A process according to any one of claims 1 to 10, wherein the temperature step is between 800 ° C and 1050 ° C.

The process of claim 11, wherein the temperature plateau is greater than 900 ° C.

13. A carbonitriding furnace (10) for receiving, in a chamber (14), a steel part, comprising gas introduction (22, 24, 26, 28) and gas extraction (18, 20), and a control module (40) adapted to control the gas introduction and gas extraction circuits for introducing, during the first and second stages, a carburising gas into the chamber only during the first steps and a nitriding gas in the chamber only during the second stages, at least one of the second stages being situated between two first stages, and adapted to maintain the pressure in the chamber during at least a portion of the two first steps to a first value and the pressure in the chamber during at least a portion of said second step between the first two steps to a second value strictly greater than the first value.

The carbonitriding furnace according to claim 13, further comprising a heating element (38) and wherein the control module (40) is adapted to control the heating element (38) to maintain the room (16). ) at a temperature step.