Process for unbinding a green part

Abstract

A process for debinding a green part in which powder particles are held together by a polymer compound, the process comprising a heat treatment of the green part under a non-oxidizing atmosphere, and a thermochemical treatment of the green part under an oxidizing atmosphere for a duration less than or equal to a predetermined time, the heat treatment and the thermochemical treatment being carried out in the same chamber and at temperatures below the sintering temperature (Tf) of the powder particles. Figure for the abstract: Fig. 2

Description

Title of the invention: Method for unbinding a green part technical field

[0001] This presentation relates to the field of additive manufacturing, and more particularly to an indirect additive manufacturing process using binder spraying onto a powder bed. This presentation focuses specifically on a process for debinding a green part. Such a debinding process can be used, in particular but not exclusively, for the additive manufacturing of aeronautical or aerospace parts. Previous technique

[0002] Additive manufacturing refers to all the techniques that allow a part to be manufactured not by removing material, but by successively adding material until the desired shape of the part is created. These techniques offer numerous advantages, including the ability to manufacture parts that could not be manufactured by other processes.

[0003] There are various additive manufacturing processes, such as laser powder bed fusion (LPBF). Recently, indirect additive manufacturing by spraying binder onto powder beds (possibly onto metal or ceramic powder, in which case it is referred to as MBJ or CBJ - in English "Metal Binder Jetting" or "Ceramic Binder Jetting" respectively) has been developed, which offers other industrial advantages, such as the possibility of producing a large number of parts by printing or of producing crack-free parts in non-weldable materials which, in the case of LPBF, would exhibit hot or cold cracking.

[0004] In indirect additive manufacturing by powder bed deposition, a powder bed is formed on a substrate, and then a binder is sprayed onto a surface of this powder bed corresponding to a cross-section of the part to be manufactured. This binder dries at least partially, for example, by heating the surface of the powder bed with an infrared lamp. Then, a new powder bed is deposited on top of the previous powder bed, and so on until the entire shape of the part to be manufactured is reconstituted. Next, the binder is crosslinked into a solid polymer to ensure that the part, which is then called a crosslinked part or "green part," has sufficient mechanical strength to withstand depowdering, an operation aimed at removing the excess powder from the part not bound by polymer. After depowdering, the green part is debound (the polymer is removed) and then sintered, which yields the final part.

[0005] Comparative tests, however, have shown that the material integrity of parts obtained by indirect additive manufacturing using binder spraying onto a powder bed was not as good as that of similar parts obtained by simple sintering from the same powder, characterized by a certain chemical composition and particle size distribution. The invention aims to at least partially overcome these drawbacks. Description of the invention

[0006] In this perspective, the inventors observed that the only difference between conventional sintering and an indirect additive manufacturing process was that the powder particles were not in contact with the binder, and that the sintered parts from the indirect additive manufacturing process could, depending on the debinding conditions, exhibit either significant porosity linked to the adsorption of oxygen on the surface of the particles during debinding, which generates PPBs (from the English "Prior Particle Boundaries", surfaces of the original particles) of oxides on the surface of the particles, or, when debinding is carried out under a non-oxidizing atmosphere, large carbides which form during sintering and which significantly impact the hardness of the sintered part.

[0007] There is therefore a need for a new unbinding process.

[0008] To this end, the present exposition relates to a method for debinding a green part (or crosslinked part) in which powder particles are held together by a polymer compound, the process comprising heat treatment of the green part under a non-oxidizing atmosphere, and thermochemical treatment of the green part under an oxidizing atmosphere for a period less than or equal to a predetermined time, the heat treatment and the thermochemical treatment being carried out in the same enclosure and at temperatures below the sintering temperature of the powder particles.

[0009] The powder particles may be metallic or metallic alloy particles, for example, particles of a nickel-based superalloy such as Inconel 718 (registered trademark) or stainless steel. In other embodiments, the powder particles may be intermetallic or non-oxide ceramic particles, such as nitrides, carbides, etc. The polymer compound is the compound resulting from the crosslinking of the binder after drying; this compound may comprise, or even consist of, mostly or entirely, one or more polymers.

[0010] The heat treatment and thermochemical treatment are carried out at temperatures below the sintering temperature of the powder particles, that is to say, at temperatures below the temperature at which the powder particles, all other conditions being equal, are likely to sinter with each other. the others. The debinding process therefore concerns debinding in the strict sense, excluding sintering.

[0011] The heat treatment includes at least one temperature variation relative to the initial temperature of the green part (e.g., ambient temperature), for example, at least one temperature increase and / or at least one temperature decrease, and / or maintaining the green part at a temperature different from ambient temperature. This temperature program is implemented under a non-oxidizing atmosphere, i.e., a gas or mixture of gases nominally containing no oxidizing compounds such as dioxygen, regardless of any compounds that may be released into this atmosphere due to the degradation of the polymer compound chains. Thus, heat treatment under a non-oxidizing atmosphere allows the polymer compound chains to degrade without the atmosphere supplying oxygen to be adsorbed onto the surface of the particles.However, heat treatment alone is generally not sufficient to degrade the polymer compound in its entirety: carbonaceous residues remain which tend to precipitate with the carbide-forming elements of the material during sintering.

[0012] The thermochemical treatment includes at least one temperature variation relative to the initial temperature of the green part (e.g., ambient temperature), for example, at least one temperature increase and / or at least one temperature decrease, and / or holding the green part at a temperature different from ambient temperature (e.g., at most, the final temperature of the heat treatment). The thermochemical treatment is carried out under conditions that allow a chemical reaction of the polymer compound to be coupled to the temperature program, in particular the combustion of carbon or carbon chains under an oxidizing atmosphere, in order to further remove the polymer compound. This avoids the presence of carbon residues in the debound part, which would otherwise impair the mechanical properties of the part after sintering.An oxidizing atmosphere refers to a gas or mixture of gases nominally comprising at least one oxidizing compound, such as dioxygen, independently of any compounds that may be released into that atmosphere due to the degradation of the polymer compound chains.

[0013] The temperature program followed during heat treatment may be different from the temperature program followed during thermochemical treatment.

[0014] Thanks to the fact that the thermochemical treatment is carried out for a duration less than or equal to a predetermined time, the thermochemical treatment is short enough to allow the polymer compound to be treated without generating excessive oxidation of the powder particles, which would also limit densification during sintering. The predetermined duration could be, for example, 1 hour, Preferably 30 minutes, preferably 5 minutes, or even preferably 3 minutes.

[0015] Furthermore, the heat treatment and thermochemical treatment are carried out in the same chamber. The chamber can be a furnace or similar device, or any device that allows a temperature program to be applied to the part while controlling the atmosphere and pressure within it. Thanks to these arrangements, the green part does not leave the chamber between the heat treatment and the thermochemical treatment. This prevents the part from absorbing moisture and avoids handling the partially debinded part, which is very fragile at this stage. Optionally, it also allows for temperature continuity between the heat treatment and the thermochemical treatment (typically preventing sudden cooling of the part), which increases process control and accelerates the debinding process.

[0016] Together, these arrangements ensure efficient removal of the polymer compound while limiting oxidation on the particle surface. Consequently, there is neither carbide precipitation during sintering, nor the formation of large oxides that surround the powder particles and hinder densification during sintering by obstructing (diffusion barrier) the formation of material necks between particles. The present debinding process thus makes it possible to obtain good densification during sintering and, ultimately, good material integrity of the sintered part and good mechanical properties, particularly hardness.

[0017] In some embodiments, the heat treatment precedes the thermochemical treatment. This allows the polymer compound to be degraded (breakage of carbon chains) before the chemical reaction. The chemical reaction of the thermochemical treatment is therefore more efficient. In other embodiments, the heat treatment is carried out after the thermochemical treatment.

[0018] In some embodiments, the heat treatment includes applying an increasing temperature to the green part, for example, according to a ramp. A temperature ramp refers to a linear variation of the temperature. The temperature thus controlled (programmed temperature or setpoint temperature) can be the temperature inside the enclosure, for example, at a reference point, ideally located near the green part, as close to it as possible. A thermocouple or other temperature sensor can be placed at the reference point. For example, a ramp rate can be between 1°C / min and 10°C / min, and preferably between 5°C / min and 10°C / min. According to other examples, the rate of temperature growth can be greater than or equal to 5°C / min, preferably 6°C / min, preferably 7°C / min, preferably 8°C / min, preferably 9°C / min, preferably 10°C / min, preferably even 12°C / min.A rapid temperature increase not only accelerates the debinding process, but also... This is interesting from an industrial standpoint, but it also limits the time the green part is exposed to oxygen released by the breakdown of certain polymer chains. By doing so, oxygen adsorption on the surface of the powder particles is even better controlled. As a complement to, or replacement for, the heat treatment ramp, the process can include applying a temperature plateau to the green part. A temperature plateau refers to maintaining a constant temperature, within a certain tolerance.

[0019] In some embodiments, the thermochemical treatment includes applying a temperature plateau to the green part. In addition to or instead of the plateau, the thermochemical treatment may include applying a temperature ramp to the green part.

[0020] In some embodiments, the end temperature of the heat treatment is less than or equal to the start temperature of the thermochemical treatment.

[0021] In certain embodiments, the atmospheres of the heat treatment and the thermochemical treatment may have all or some of the following characteristics, independently of each other: - the non-oxidizing atmosphere is an atmosphere of argon or hydrogenated argon, or of dihydrogen or helium, or a secondary vacuum; - an oxidizing atmosphere is an atmosphere of air, in particular dry air, for example synthetic air (80% N2 and 20% O2); - the oxidizing atmosphere comprises a mixture of dioxygen with a neutral gas; - the non-oxidizing atmosphere is renewed during the heat treatment; - the oxidizing atmosphere is renewed during the thermochemical treatment.

[0022] A renewed atmosphere refers to an atmosphere that is extracted from the enclosure for treatment and made closer to its nominal composition (possibly its original composition) before being reintroduced into the enclosure. Renewing an atmosphere allows for better control of the chemical reactions within the enclosure.

[0023] In some embodiments, the predetermined duration is less than or equal to the duration of the heat treatment. Thus, the thermochemical treatment is shorter than the heat treatment. This further limits undesirable oxidation of the part during debinding.

[0024] In some embodiments, the polymer is an organic polymer, for example thermoplastic or thermosetting.

[0025] In certain embodiments, the predetermined time is the shortest time that reduces the additional carbon content of the debound part, measured by inductively coupled plasma mass spectrometry (ICP-MS), to a value below 1000 ppm, preferably below 600 ppm, preferably even below 400 ppm, and preferably even below 200 ppm, relative to the original composition of the powder particles. Inductively coupled plasma mass spectrometry, also known as ICP-MS, is a well-established physical method for chemical analysis that allows for the simultaneous quantification of virtually all chemical elements. Because the predetermined time is defined in this way, the thermochemical treatment can be relatively rapid and offers a good compromise between the disappearance of the polymer compound and the absence of oxygen adsorbed onto the surface of the particles in the debound part.

[0026] Alternatively or in addition, the predetermined duration is defined such that the oxygen content acquired by the debinding part during the debinding process, relative to the original composition of the powder particles, is less than or equal to 2800 ppm, preferably less than 2400 ppm. This acquired oxygen may originate from the oxidizing atmosphere but also from the degradation of the polymer compound, more precisely the oxygen released by the breaking of certain chains of the polymer compound, excluding the oxygen initially contained in the powder particles.

[0027] The present description also relates to an indirect additive manufacturing process, comprising obtaining a green part in which powder particles are held together by a polymer compound, debinding the green part by the debinding process described above, and sintering the debinded part. Thanks to the proposed debinding, this manufacturing process makes it possible to obtain sintered parts with good material health and good mechanical properties, particularly hardness.

[0028] In some embodiments, sintering immediately follows debinding. This allows the heat generated by the thermal or thermochemical treatment to initiate sintering, which is very efficient on an industrial scale. Furthermore, sintering can take place in the same chamber as debinding to avoid further handling and contamination of the debinded part.

[0029] The present disclosure also relates to a part obtained by the indirect additive manufacturing process described above, in which the oxygen mass fraction measured by inductively coupled plasma mass spectrometry is less than 0.41%, preferably 0.35%, preferably 0.1%, preferably 0.06%, and / or the carbon mass fraction measured by inductively coupled plasma mass spectrometry is less than 0.11%, preferably 0.08%, and / or the porosity is less than 2%. The part, having undergone sintering, may also be called a "sintered part" by opposition to the part in states prior to sintering. The oxygen, carbon and / or porosity levels are such that such a part has necessarily been debinded by the controlled debinding process as proposed in this presentation. Brief description of the drawings

[0030] Other features and advantages of the object of this presentation will become apparent from the following description of embodiments, given by way of non-limiting examples, with reference to the attached figures.

[0031] Fig. 1 schematically illustrates the steps of an indirect additive manufacturing process by spraying binder onto a powder bed according to one embodiment.

[0032] Fig. 2 is a graph illustrating, not necessarily to scale, the temperature variation of an enclosure as a function of time for a debinding process according to a first embodiment.

[0033] Fig. 3 is a graph illustrating the mass loss of a green part as a function of time during the debinding process according to the first embodiment and according to a comparative example, as well as the mass gain measured on the powder, also called blank, according to the first embodiment.

[0034] Fig. 4 is a graph illustrating, not necessarily to scale, the temperature variation of an enclosure as a function of time for a debinding process according to a second embodiment. Detailed description

[0035] The principle of an indirect additive manufacturing process by binder spraying onto a powder bed is illustrated in [Fig. 1]. The process comprises the formation of successive powder beds 14 on a support 12. Each powder bed 14 is formed on the preceding powder bed, except for the first powder bed, which may be in direct contact with the support 12.

[0036] The powder may be a metallic powder, for example, an iron-nickel alloy such as Inconel 718 (registered trademark, the composition of which is detailed in Table 1, excluding unavoidable impurities). However, other materials may be considered, such as stainless steel like SS316L (the composition of which is detailed in Table 2, excluding unavoidable impurities). Unless otherwise stated, in this description, the fractions mentioned are mass fractions.

[0037] [Tables 1] Elements C Mn PS Si Cr Ni Mo O Min (% mass) 0.02 - - - - 17 50 2.8 - Max 0.08 0.35 0.015 0.015 0.35 21 55 3.3 0.06 (% mass) Elements B Ti Ta Nb Cu Co Al Fe Min (% mass) - 0.6 - 4.75 - - 0.2 - Max (% mass) 0.006 1.2 0.05 5.50 0.3 1 0.8 Complement

[0038] [Tables2 Elements C Mn PS Si Cr Ni Mo Min (% mass) - - - - - 16 9 1.5 Max (% mass) <0.03 <2 <0.01 <0.005 1 19 13 3 Elements NO Fe Min (% mass) - - - Max (% mass) <0.003 <0.002 Complement

[0039] In the examples above, the low levels of oxygen and carbon are noted. In general, the powder material can be selected with the lowest possible oxygen and / or carbon content to limit oxygen adsorption and carbide formation during the additive manufacturing process. Typically, the initial oxygen content of the powder used can be limited by using atomization processes such as plasma rotating electrode process (PREP). For example, the oxygen content of the powder particles can be less than 500 ppm, or even less than 150 ppm, and preferably less than 50 ppm.

[0040] The process also includes the selective application of binder onto each of the powder beds 14. Thus, after the formation of a powder bed, a binder 16 is applied to this powder bed 14 before the formation of the next powder bed 14. The binder 16 can be applied by a print head 18, for example, in the form of droplets. The application is said to be selective in that the application of binder 16 may not be made over the entire powder bed 14, but only onto a surface that is to be printed and which corresponds to a cross-section of the part to be manufactured. Such a surface can be defined in a CAD (computer-aided design) file.

[0041] The binder 16 may comprise one or more solvents and one or more polymers in solution in all of these solvents. Typically, the polymer may be an organic polymer, for example, a thermoplastic or thermosetting polymer. For example, the binder may be a mixture of water, ethylene glycol, and 2-butoxyethanol (3 solvents) with polyvinylpyrrolidone (1 polymer).

[0042] The binder 16 seeps into the powder bed 14 and can then undergo natural drying 20 (typically at room temperature) or forced drying (drying activated by a heat source such as an infrared lamp), during which the binder, and in particular its solvents, partially evaporates. For example, the drying temperature can be between 25°C and 70°C. A pause time, for example on the order of several seconds, can be observed between the infiltration of the binder 16 and the start of drying.

[0043] As shown schematically by arrow 22, these steps can be repeated, with a new bed of powder 14 being deposited on the bed of powder which has previously received binder, until the shape of the part to be manufactured, thus built layer by layer, is entirely imprinted.

[0044] After the part has been printed layer by layer, a crosslinking step allows the binder to finish drying (typically, the solvents to finish evaporating) and the polymer(s) to polymerize. For the sake of brevity, the term polymer compound is used to refer to the compound, consisting mainly or entirely of one or more crosslinked polymer(s), which ensures the cohesion of the powder particles. This results in a green part 24 that is generally a single piece, while the remaining unprinted powder 26 remains in a granular state. For example, crosslinking can be carried out at a temperature of 200°C for 12 hours, under air. After crosslinking, the green part 24 must have a sufficiently high tensile strength to withstand the subsequent steps.For example, to withstand the handling required for powder removal, it is preferable for the part to have a four-point bending equivalent tensile strength (standard test) greater than or equal to 5, 6, or 7 MPa, or even 20, 21, or 22 MPa for more complex parts; otherwise, the part is highly likely to be damaged during powder removal. The term "equivalent tensile strength" is used because the formula for calculating the stress in this test applies to dense materials, which is not the case for parts to be coated. For example, after crosslinking, the polymer compound may contain between 50 and 60% carbon and between 20 and 30% oxygen, with additional constituents typically including nitrogen and hydrogen.

[0045] The green part 24 then undergoes depowdering, which can be carried out in a manner known per se, consisting of removing from the green part 24 the unprinted powder residues 26. For example, the depowdering can be carried out using an air nozzle compressed (typically with a maximum pressure of 2 bar). Next, the green part 24 is debinded and then sintered. As illustrated in [Fig. 1], debinding can be carried out by placing the green part 24 in a chamber 28. Debinding may include one or more heat treatments and thermochemical treatments of the green part 24 at a temperature higher than the binder's crosslinking temperature, as will be detailed later.

[0046] After debinding, the part referred to as the brown part 25 (or debinded part) can be sintered, either in the same chamber 28 or in a different chamber. For example, sintering can be carried out at a temperature below the solidus, for example, around 1220°C for Inconel 718 (registered trademark), whose solidus is 1260°C, or at a slightly higher temperature, but in any case remaining below the liquidus temperature. The atmosphere in the chamber 28 can be a secondary vacuum (pressure below 105 mbar), argon with 5% dihydrogen by volume, pure dihydrogen, or a helium atmosphere. Oxygen traps (getters) can be present in the chamber 28, for example, a highly oxygen-averse alloy, particularly a titanium-based alloy such as TA6V.

[0047] Sintering allows the brown part 25 to be densified to obtain the final part 30. The final part 30 can then be cooled, for example in the enclosure 28 or outside. If necessary, the final part 30 can then be finished, as shown in the last step of [Fig. 1].

[0048] A first embodiment of a debinding process is described with reference to Figures 2 and 3. Without loss of generality, the debinding process applied to a green part made of Inconel 718 (registered trademark) is subsequently described, but the principles described below are applicable to other materials. As described previously, the green part 24 is such that the powder particles are held together by the crosslinked polymer compound.

[0049] In the first embodiment, the debinding process comprises a heat treatment of the green part 24 under a non-oxidizing atmosphere, in the chamber 28, at temperatures below the sintering temperature Tf of the powder particles, which itself is below the solidus temperature Ts of the alloy, in this example. The temperature variation applied to the green part may include the application of an increasing temperature, for example, according to a temperature ramp 32. However, the temperature increase could be non-linear, or interspersed with temperature plateaus. The slope of the ramp is, for example, between 1°C / min and 10°C / min, preferably between 5°C / min and 10°C / min, preferably about 10°C / min.

[0050] In this case, the heat treatment begins at time t0 and lasts until time t1. During this period, which can range from 30 minutes to 7 hours, preferably between 40 For a further 45 minutes and 1 hour, preferably for another 45 minutes, the atmosphere within the chamber is non-oxidizing, specifically devoid of oxygen. For example, the non-oxidizing atmosphere can be an atmosphere of argon or hydrogenated argon, or even helium, or a primary or secondary vacuum. To preserve its characteristics, the non-oxidizing atmosphere can be renewed periodically or continuously during the heat treatment. The renewal rate of the non-oxidizing atmosphere can be between 1 L / h and 30 L / h, preferably between 2 L / h and 10 L / h, and preferably between 3 L / h and 5 L / h.

[0051] The debinding process also includes, preferably after heat treatment, a thermochemical treatment of the green part 24 in the same chamber 28, at temperatures below the sintering temperature Tf of the powder particles. The green part 24 advantageously remains in the chamber 28 between the heat treatment and the thermochemical treatment.

[0052] The thermochemical treatment is carried out under an oxidizing atmosphere, i.e., one containing oxygen in a form suitable for reacting with the green part 24, in particular with the polymer compound. For example, the oxidizing atmosphere may be a dry air atmosphere, such as synthetic air, or comprise a mixture of oxygen with a neutral gas (typically argon or nitrogen), typically having a mixture of 80% nitrogen and 20% oxygen (volume fractions). The oxygen content may, however, be modified, for example, to be between 10% and 25% (volume fractions). In order to maintain its characteristics, the oxidizing atmosphere may be renewed periodically or continuously during the heat treatment. An oxidizing atmosphere renewal rate can be between 1 L / h and 30 L / h, preferably between 2 L / h and 10 L / h, preferably still between 3 L / h and 5 L / h.

[0053] The thermochemical treatment is applied to the green part for a duration less than or equal to a predetermined time, in order to allow the chemical reaction of the polymer compound with atmospheric oxygen without causing oxidation or excessive oxygen adsorption on the surface of the powder particles. For example, the predetermined time is less than or equal to the duration of the heat treatment; in other words, the thermochemical treatment is shorter than or the same duration as the heat treatment.

[0054] In [Fig. 2], the temperature program applied during the thermochemical treatment is illustrated as a temperature plateau 34 at a temperature above ambient temperature. More precisely, the starting temperature of the thermochemical treatment can be greater than or equal to the ending temperature of the heat treatment; in this case, a continuity of temperature is even observed between the end of the heat treatment and the beginning of the thermochemical treatment. The temperature of the thermochemical treatment is typically between 430°C and 490°C, preferably between 460°C and 480°C, preferably around 470°C.

[0055] As an alternative or in addition to the temperature step 34, the thermochemical treatment could include a temperature ramp, with a slope greater than, less than or equal to that of the heat treatment, or any other temperature program allowing the disappearance of the polymer compound by thermochemical means.

[0056] In [Fig. 2], the thermochemical treatment begins at time t1 and lasts until time t2. The duration t2-t1 of the thermochemical treatment can be between 3 minutes and 1 hour, preferably between 4 and 10 minutes, preferably about 5 minutes. As previously stated, the duration t2-t1 of the thermochemical treatment can be less than or equal to the duration t1-t0 of the heat treatment. Overall, the proposed debinding process can have a duration t2-t0 of one hour or less.

[0057] After the thermochemical treatment, the green part 24 can be cooled. This is illustrated by a decreasing temperature ramp 36 in [Fig. 2], starting from time t2, the end of the thermochemical treatment. Although shown here as linear, the temperature decrease could be non-linear or interrupted by temperature plateaus. The green part 24 can be brought back to room temperature before continuing the indirect additive manufacturing process. At this stage, before the sintering step, a so-called debinded or brown part 25 is obtained.

[0058] Figure 3 illustrates the relative mass loss Am / mO (in %, left axis of the figure) with respect to the initial mass of the green part 24 as a function of time during the debinding process according to a comparative example (curve 37) and according to the first embodiment (curve 38). Curves 37 and 38 were obtained for similar but distinct green parts.

[0059] As shown in [Fig. 3], the mass of the green part 24 decreases during the heat treatment, between t0 and t1, which corresponds to the pyrolysis of the polymer compound, both for the first embodiment (curve 38) and for the comparative example (curve 37). Towards the end of the heat treatment, the mass loss may slow down. A difference in mass loss, denoted A in [Fig. 3], may appear between the parts because these parts may contain slightly different quantities of polymer compound due to the coating step (powder bed compaction gradient) and the printing step, which result in heterogeneous infiltration of the binder within the powder bed, hence different quantities of polymer compound to be degraded during debinding.

[0060] At time t1, the heat treatment of the comparative example (curve 37) continues under the same atmosphere, until the end of the debinding process, and does not allow for a further reduction in the mass of the part at vert 24, while the The heat treatment of the first embodiment (curve 38) is followed immediately by the thermochemical treatment, which results in a further significant mass loss. Around time tl (in [Fig. 3]: immediately after tl), a short lag can be observed due to the purging of the non-oxidizing atmosphere and its replacement by the oxidizing atmosphere. This second phase of mass loss, which also contributes to the final deviation B compared to the comparative example (curve 37), is linked to the chemical reaction of the polymer compound during the thermochemical treatment, a reaction whose products are mostly released into the atmosphere. The mass loss can then slow down once most of the polymer compound has been removed from the part at green 24.At this stage, the additional carbon content of the green part 24, measured by inductively coupled plasma mass spectrometry, is preferably less than 1000 ppm, preferably less than 600 ppm, preferably less than 400 ppm, preferably less than 200 ppm, relative to the original composition of the powder particles.

[0061] In reality, the green part 24, during debinding, undergoes a slight mass gain due to the uptake of oxygen from the oxidizing atmosphere by the green part 24. The mass gain measured on the powder alone in the absence of the polymer compound, sometimes called "blank" and illustrated by curve 39 in [Fig. 3] (right axis), was quantified separately and subtracted from curve 38 in [Fig. 3]. Thus, curve 39 in [Fig. 3] represents only the mass gain related to the surrounding atmosphere and not to oxygen from the degradation of the polymer compound, since the "blank" is measured on powder in the absence of the polymer compound. As can be seen from curve 39, the mass gain in the absence of polymer is less than 200 ppm during the heat treatment, and therefore very limited. This is evaluated by thermogravimetric analysis and additional ICP measurements in oxygen and, if necessary, in carbon.

[0062] Ideally, the thermochemical treatment is stopped before oxidation and oxygen adsorption become excessive, for example by replacing the oxidizing atmosphere with a non-oxidizing atmosphere such as a vacuum at the desired level. The predetermined duration, which sets the upper limit for the duration of the thermochemical treatment, may be less than or equal to the time required to obtain the aforementioned carbon levels. Thanks to these provisions, the oxygen mass gain, compared to the original composition of the powder particles, can be limited to a value less than or equal to 2800 ppm, preferably 2400 ppm. Furthermore, since the oxygen present in the polymer compound contributes significantly to the contamination of the powder particles during debinding, it is advantageous to minimize the oxygen content of the polymer compound, for example by using a binder with a monomer depleted in oxygen atoms. More generally, the Oxygen mass gain can be further reduced by selecting a binder whose polymer compound is unlikely to release oxygen during debinding, and / or by limiting binder saturation (amount of binder, depending in particular on the number of print head passes per powder bed) of the part during the printing step.

[0063] The sintered part 30 obtained from the green part thus debinded has good material health and good mechanical properties: on the one hand, the small amount of oxygen absorbed by the powder after debinding results in good density and efficient sintering thanks to the rapid formation of material necks. On the other hand, the very low quantity of carbon residues prevents the formation of niobium- or titanium-rich carbides during sintering, which typically allows the niobium to participate in the precipitation of the hardening phase y” - Ni3Nb, which contributes significantly to the hardness of the material.

[0064] The sintered part 30 thus obtained is such that the mass fraction of oxygen measured by inductively coupled plasma mass spectrometry is less than 0.41%, preferably 0.35%, preferably 0.1%, preferably 0.06%. Furthermore, the mass fraction of carbon measured by inductively coupled plasma mass spectrometry is less than 0.11%, preferably 0.08%. Moreover, the porosity is less than 2% (porosity always being expressed as a volume fraction, by definition).

[0065] For example, a part made of Inconel 718 manufactured by the indirect additive manufacturing process described above has a hardness between 34 and 44 HRC (Rockwell C hardness) and an average grain size corresponding to ASTM No. 5 or finer (in accordance with the requirements of AMS 5917:2017), which is permitted by complete debinding avoiding the precipitation of carbides or oxides at grain boundaries.

[0066] Figure 4 shows a debinding process according to a second embodiment. In this figure, elements corresponding to or identical to those of the first embodiment will be given the same reference symbol, up to the tens digit, and will not be described again.

[0067] According to the second embodiment, the debinding process comprises a heat treatment including a temperature ramp 42, from time t0 to time t1, immediately followed by a thermochemical treatment including a temperature plateau 44, from time t1 to time t2. The second embodiment differs from the first in that the sintering of the part immediately follows the debinding, optionally in the same chamber 28. For this purpose, instead of cooling the debinded part according to the ramp 36, a secondary vacuum is created in the chamber 28 from time t2 to time t3. During this time, the part is maintained at a temperature plateau 46, for example at the same temperature as the temperature plateau 44 of the thermochemical treatment, and in any case maintained at Temperatures below the sintering temperature Tf are used. Once the desired vacuum level is reached, identified by time t3, the temperature in chamber 28 can be increased to reach the sintering temperature Tf without ever exceeding the liquidus temperature of the alloy (in the case of super-solidus sintering), or even the solidus temperature Ts of the alloy, thus sintering the powder particles. The sintering process can then be carried out by a person skilled in the art, according to their expertise.

[0068] Although the present description refers to specific embodiments, modifications may be made to these examples without departing from the general scope of the invention. Furthermore, individual features of the various embodiments illustrated or mentioned may be combined in additional embodiments. Therefore, the description and drawings should be considered in an illustrative rather than restrictive sense.

Claims

Demands

1. A method for debinding a green part (24) in which powder particles are held together by a polymer compound, the method comprising a heat treatment of the green part under a non-oxidizing atmosphere, and a thermochemical treatment of the green part under an oxidizing atmosphere for a time less than or equal to a predetermined time, the heat treatment and the thermochemical treatment being carried out in the same enclosure (28) and at temperatures below the sintering temperature (Tf) of the powder particles.

2. Debinding process according to claim 1, wherein the heat treatment precedes the thermochemical treatment.

3. Debinding method according to claim 1 or 2, wherein the heat treatment comprises applying increasing temperature to the green part, for example along a ramp (32, 42); optionally wherein the rate of temperature increase is greater than 5°C / min.

4. Debinding method according to any one of claims 1 to 3, wherein the thermochemical treatment comprises applying a temperature step (34, 44) to the green part.

5. Debinding process according to any one of claims 1 to 4, wherein the end temperature of the heat treatment is less than or equal to the start temperature of the thermochemical treatment.

6. A debinding process according to any one of claims 1 to 5, wherein the non-oxidizing atmosphere is an atmosphere of argon or hydrogenated argon or dihydrogen or helium or a secondary vacuum, and / or the oxidizing atmosphere is an atmosphere of air, for example synthetic air, and / or the oxidizing atmosphere comprises a mixture of oxygen with a neutral gas, and / or wherein the non-oxidizing atmosphere is renewed during the heat treatment and / or wherein the oxidizing atmosphere is renewed during the thermochemical treatment.

7. A debinding method according to any one of claims 1 to 6, wherein the predetermined time is less than or equal to the heat treatment time, and / or wherein the cumulative time of the Thermal treatment and thermochemical treatment is less than or equal to one hour.

8. A debinding method according to any one of claims 1 to 7, wherein the polymer is an organic polymer, for example thermoplastic or thermosetting.

9. A debinding method according to any one of claims 1 to 8, wherein the predetermined time is the shortest time that reduces the additional carbon content of the debinded part, measured by inductively coupled plasma mass spectrometry, to a value of less than 1000 ppm, preferably less than 600 ppm, preferably still less than 400 ppm, preferably still less than 200 ppm, relative to the original composition of the powder particles.

10. A debinding process according to any one of claims 1 to 9, wherein the predetermined time is defined such that the oxygen content acquired by the debinding part during the debinding process, relative to the original composition of the powder particles, is less than 2800 ppm, preferably 2400 ppm, said oxygen content arising from the degradation of the polymer compound and the oxidizing atmosphere.

11. Indirect additive manufacturing process, comprising obtaining a green part (24) in which powder particles are held together by a polymer compound, debinding the green part (24) by the debinding process according to any one of claims 1 to 9, and sintering the debinded part, optionally wherein the sintering immediately follows the debinding, preferably in the same chamber (28).

12. Part (30) obtained by the indirect additive manufacturing process according to claim 10, wherein the mass fraction of oxygen measured by inductively coupled plasma mass spectrometry is less than 0.41%, preferably 0.35%, preferably 0.1%, preferably 0.06%, and / or the mass fraction of carbon measured by inductively coupled plasma mass spectrometry is less than 0.11%, preferably 0.08%, and / or the porosity is less than 2%.

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