EP0029389B1 - Process for producing shaped articles from spherical metal-particle powders - Google Patents
Process for producing shaped articles from spherical metal-particle powders Download PDFInfo
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- EP0029389B1 EP0029389B1 EP80401633A EP80401633A EP0029389B1 EP 0029389 B1 EP0029389 B1 EP 0029389B1 EP 80401633 A EP80401633 A EP 80401633A EP 80401633 A EP80401633 A EP 80401633A EP 0029389 B1 EP0029389 B1 EP 0029389B1
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- compaction
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- 239000000843 powder Substances 0.000 title claims description 48
- 238000000034 method Methods 0.000 title claims description 16
- 239000002923 metal particle Substances 0.000 title description 4
- 238000005056 compaction Methods 0.000 claims description 26
- 239000000203 mixture Substances 0.000 claims description 25
- 229920000609 methyl cellulose Polymers 0.000 claims description 12
- 239000001923 methylcellulose Substances 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 238000005245 sintering Methods 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 239000000314 lubricant Substances 0.000 claims description 9
- 239000011230 binding agent Substances 0.000 claims description 8
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 8
- 229920002134 Carboxymethyl cellulose Polymers 0.000 claims description 5
- 239000001768 carboxy methyl cellulose Substances 0.000 claims description 5
- 235000010948 carboxy methyl cellulose Nutrition 0.000 claims description 5
- 230000007935 neutral effect Effects 0.000 claims description 5
- 229910001338 liquidmetal Inorganic materials 0.000 claims description 4
- 239000013528 metallic particle Substances 0.000 claims description 3
- 238000003475 lamination Methods 0.000 claims 1
- 235000010981 methylcellulose Nutrition 0.000 claims 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 10
- 239000007789 gas Substances 0.000 description 9
- 239000002245 particle Substances 0.000 description 8
- 239000007787 solid Substances 0.000 description 6
- 229910000831 Steel Inorganic materials 0.000 description 5
- 238000005242 forging Methods 0.000 description 5
- 239000010959 steel Substances 0.000 description 5
- 238000005096 rolling process Methods 0.000 description 4
- 229910045601 alloy Inorganic materials 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- 238000000889 atomisation Methods 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000000470 constituent Substances 0.000 description 3
- 229910002804 graphite Inorganic materials 0.000 description 3
- 239000010439 graphite Substances 0.000 description 3
- 238000010348 incorporation Methods 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 229910052750 molybdenum Inorganic materials 0.000 description 3
- 229910000851 Alloy steel Inorganic materials 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 229910001347 Stellite Inorganic materials 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 229910052804 chromium Inorganic materials 0.000 description 2
- AHICWQREWHDHHF-UHFFFAOYSA-N chromium;cobalt;iron;manganese;methane;molybdenum;nickel;silicon;tungsten Chemical compound C.[Si].[Cr].[Mn].[Fe].[Co].[Ni].[Mo].[W] AHICWQREWHDHHF-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910052748 manganese Inorganic materials 0.000 description 2
- 239000011572 manganese Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 238000010025 steaming Methods 0.000 description 2
- UDHXJZHVNHGCEC-UHFFFAOYSA-N Chlorophacinone Chemical compound C1=CC(Cl)=CC=C1C(C=1C=CC=CC=1)C(=O)C1C(=O)C2=CC=CC=C2C1=O UDHXJZHVNHGCEC-UHFFFAOYSA-N 0.000 description 1
- 235000016936 Dendrocalamus strictus Nutrition 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000005275 alloying Methods 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 238000005256 carbonitriding Methods 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- XCNJCXWPYFLAGR-UHFFFAOYSA-N chromium manganese Chemical compound [Cr].[Mn].[Mn].[Mn] XCNJCXWPYFLAGR-UHFFFAOYSA-N 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 230000001427 coherent effect Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000010908 decantation Methods 0.000 description 1
- 238000000280 densification Methods 0.000 description 1
- 238000007580 dry-mixing Methods 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000009689 gas atomisation Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000004816 latex Substances 0.000 description 1
- 229920000126 latex Polymers 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 230000033764 rhythmic process Effects 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 230000007928 solubilization Effects 0.000 description 1
- 238000005063 solubilization Methods 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 238000009692 water atomization Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F1/00—Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
- B22F3/10—Sintering only
- B22F3/1017—Multiple heating or additional steps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
- B22F3/12—Both compacting and sintering
Definitions
- the invention relates to the manufacture of non-fragile shaped parts from powders consisting of spheroidal metal particles.
- This invention makes it possible to use these powders in applications where known techniques of mechanical compaction delivered drafts that are too fragile to be handled under industrial production conditions.
- the invention can be applied according to Belgian patent BE-A-517440, in which the cohesion is obtained by bonding by mixing before sintering the metal powder with a cellulose-based cement, such as cellulose acetate for example. In this way, a clay mass is obtained, the shaping of which takes place without significant pressure, by simple molding.
- a powder is generally used with an irregular grain shape, characterized by a specific surface related to the large particle size.
- the mechanical entanglement of grains in the compaction ensures sufficient mechanical strength for all the necessary manipulations of the tablet.
- These irregularly shaped grain powders are generally obtained by the water atomization process. This process consists of spraying a jet of liquid metal with one or more jets of water under pressure. The powder is sprayed into a water bath where it finishes cooling. After decantation, the powder is dried and undergoes a first deoxidation or reduction.
- the powder obtained has a particle size mainly below 160 micrometers.
- the grains have a shape depending on the shade and the atomization conditions, generally quite tormented.
- this powder must undergo a reduction step, its composition of alloying elements must be limited to those whose oxides are easily reducible.
- the typical grade AISI 4600 contains 2% nickel and 0.8% molybdenum.
- Chromium-manganese grades, which are less expensive, can only be produced at the cost of an expensive carbon reduction treatment at 1200 ° C. followed by grinding of the sintered powder.
- the neutral gas atomization process makes it possible to completely overcome this problem of composition.
- This process involves spraying a jet of liquid metal with several jets of pressurized gas.
- the solidification of the droplets and the cooling of the powder are carried out in a confined enclosure; the atomizing gas which fills the enclosure is neutral with respect to the atomized metal.
- the grade it can be either argon or nitrogen.
- the device and the atomization enclosure can advantageously be designed according to the principles of the French breveis 73-43159 of December 4, 1973 or n ° 73-45788 of December 20, 1973.
- the powder obtained has a particle size between a few microns and 500 microns , with a spheroidal grain shape.
- the variable oxygen content depending on the grade is typically of the order of 100 to 200 ppm, and the specific surface area related to the particle size is close to the minimum value of a quasi-spherical powder.
- the mechanical strength of the tablets depends on the interparticle contact surface produced during compaction. In practice, it is found that for a Vickers hardness under 500 g greater than 100, the mechanical strength and the resistance to crumbling of the tablets become insufficient to allow normal handling of these tablets, which severely limits the potential applications of these powders for making blanks by cold compaction.
- the present invention makes it possible both to overcome this severe limitation and to ensure, from powder made up of spheroidal metallic particles, the production of non-fragile shaped parts having a Vickers hardness under 500 g greater than 500.
- the principle used is the incorporation into the metal powder, by dry mixing, of an organic binder in the form of a powder of the methylcellulose type or more generally of cellulose gums which are polymers soluble in water.
- the progressive incorporation into the mixture of an amount of water equal to that of methylcellulose, that is to say from 0.2 to 2% by weight, allows the solubilization of the methylcellulose and avoids the phenomena of demixing of the different constituents of the mixture, such as graphite powder, solid lubricant powder, etc.
- the mixture is then ready for use and provides the tablets with mechanical strength and sufficient crumbling resistance for normal handling with compacting pressures of 25 to 75 daN / mm 2 . These properties can be increased, if necessary, by a steaming treatment at 120 ° C.
- the elimination of this organic binder is ensured during sintering by a heat treatment under a neutral or reducing atmosphere comprising a plateau between 300 and 500 ° C., the actual sintering being carried out under the same atmosphere under the conditions of time and temperature required by the application and the shade.
- the dosages on sintered product indicate an increase in the carbon content of less than 0.2 times the content of the initial mixture in methylcellulose and no variation in the oxygen content compared to the gas atomized powder.
- the powder consisting of spheroidal metal particles used can advantageously be obtained by atomization of liquid metal by means of gaseous jets.
- the cellulose gum used can advantageously be methylcellulose.
- test pieces compacted under 75 daN / mm 2 have a flexural breaking strength of 0.200 daN / mm 2 . After baking at 120 ° C, the flexural strength increases to 0.400 daN / mm 2 . These values allow handling of the tablets without special precautions. In addition, the use of hydrolyzed methylcellulose as a compaction binder brings a spectacular improvement in the resistance to the erosion of the edges and the sufaces of the tablets.
- the annular compaction was carried out at 40 daN / mm 2 with an industrial mechanical press.
- the density obtained is 6.4 g / cm 3 .
- the filling of the powder and the ejection of the blank were carried out automatically at rhythm of 400 pieces / hour.
- the tablets produced from mixtures without hydrolyzed methylcellulose are very friable and cannot be handled, even after compression under 150 daN / mm 2 .
- a practically complete densification of these tablets could be obtained by a heat treatment under vacuum comprising a plateau between 300 and 500 ° C. and a sintering at high temperature depending on the structure to be obtained, this temperature being able in some cases to be between 1250 ° C and 1350 ° C, for example.
- spherical blanks were produced by cold isostatic compaction.
- the powder is placed in latex molds and the molds placed in an enclosure where a hydraulic pressure of 2,000 to 3,500 bans is applied. Beads 8 to 30 mm in diameter were thus obtained which were sintered under the conditions indicated in Example 3.
- the strip passes at the same speed in a passage oven under a cracked ammonia atmosphere comprising a zone at 300-500 ° C where the organic binder is eliminated and a zone at 1150 ° C where is carried out the actual sintering.
- This strip retains a porosity of 25% by volume and can be used, for example, as a filter medium.
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- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Powder Metallurgy (AREA)
Description
L'invention concerne la fabrication de pièces de forme non fragiles à partir de poudres constituées de particules métalliques sphéroïdales.The invention relates to the manufacture of non-fragile shaped parts from powders consisting of spheroidal metal particles.
Cette invention rend possible l'utilisation de ces poudres dans les applications où les techniques connues de compaction mécanique délivraient des ébauches trop fragiles pour être manipulées dans des conditions de production industrielles.This invention makes it possible to use these powders in applications where known techniques of mechanical compaction delivered drafts that are too fragile to be handled under industrial production conditions.
Si l'on veut obtenir une tenue mécanique suffisante de la pièce avant frittage sans qu'il soit nécessaire de rendre la poudre compacte par une pression délibérée, on peut appliquer l'invention selon le brevet belge BE-A-517440, dans laquelle la cohésion est obtenue par collage en mélangeant avant frittage la poudre métallique avec un ciment à base de cellulose, tel que l'acétate de cellulose par exemple. De cette manière, on obtient une masse argileuse dont la mise en forme se fait sans pression notable, par simple moulage.If it is desired to obtain sufficient mechanical strength of the part before sintering without it being necessary to make the powder compact by deliberate pressure, the invention can be applied according to Belgian patent BE-A-517440, in which the cohesion is obtained by bonding by mixing before sintering the metal powder with a cellulose-based cement, such as cellulose acetate for example. In this way, a clay mass is obtained, the shaping of which takes place without significant pressure, by simple molding.
En revanche, pour assurer sans collage à froid la tenue mécanique et la résistance à l'effritte- ment d'un comprimé, on utilise en général une poudre avec une forme de grain irrégulière, caractérisée par une surface spécifique rapportée à la granulométrie importante. L'enchevêtrement mécanique que des grains à la compaction assure une tenue mécanique suffisante pour toutes les manipulations nécessaires du comprimé. Ces poudres à grains de forme irrégulière sont obtenues généralement par le procédé d'atomisation à l'eau. Ce procédé consiste à pulvériser un jet de métal liquide par un ou plusieurs jets d'eau sous pression. La poudre est projetée dans un bain d'eau où elle finit de refroidir. Après décantation, la poudre est séchée et subit une première désoxydation ou réduction. La poudre obtenue a une granulométrie en majeure partie inférieure à 160 micromètres. Les grains ont une forme dépendant de la nuance et des conditions d'atomisation, en général assez tourmentée. En contrepartie, cette poudre devantsubir une étape de réduction, sa composition en éléments d'alliage doit être limitée à ceux dont les oxydes sont facilement réductibles. Par exemple pour les aciers peu alliés, la nuance typique AISI 4600 contient 2% de nickel et 0,8% de molybdène. Les nuances au chrome-manganèse, moins coûteuses, ne peuvent être réalisées qu'au prix d'un traitement onéreux de réduction par le carbone à 1200° C suivi d'un broyage de la poudre frittée.On the other hand, to ensure, without cold bonding, the mechanical strength and the crumbling resistance of a tablet, a powder is generally used with an irregular grain shape, characterized by a specific surface related to the large particle size. The mechanical entanglement of grains in the compaction ensures sufficient mechanical strength for all the necessary manipulations of the tablet. These irregularly shaped grain powders are generally obtained by the water atomization process. This process consists of spraying a jet of liquid metal with one or more jets of water under pressure. The powder is sprayed into a water bath where it finishes cooling. After decantation, the powder is dried and undergoes a first deoxidation or reduction. The powder obtained has a particle size mainly below 160 micrometers. The grains have a shape depending on the shade and the atomization conditions, generally quite tormented. In return, this powder must undergo a reduction step, its composition of alloying elements must be limited to those whose oxides are easily reducible. For example for low alloy steels, the typical grade AISI 4600 contains 2% nickel and 0.8% molybdenum. Chromium-manganese grades, which are less expensive, can only be produced at the cost of an expensive carbon reduction treatment at 1200 ° C. followed by grinding of the sintered powder.
Le procédé d'atomisation par gaz neutre permet de s'affranchir totalement de ce problème de composition. Ce procédé consiste à pulvériser un jet de métal liquide par plusieurs jets de gaz sous pression. La solidification des gouttelettes et le refroidissement de la poudre s'effectuent en enceinte confinée; le gaz de pulvérisation qui remplit l'enceinte est neutre vis-à-vis du métal atomisé. Il peut s'agir suivant la nuance, soit d'argon, soit d'azote. Le dispositiv et l'enceinte d'atomisation peuvent être avantageusement conçus suivant les principes des breveis français 73-43159 du 4 Décembre 1973 ou n° 73-45788 du 20 Décembre 1973. La poudre obtenue a une granulométrie comprise entre quelques microns et 500 microns, avec une forme des grains sphéroïdale. La teneur en oxygène variable selon la nuance est tpiquement de l'ordre de 100 à 200 ppm, et la surface spécifique rapportée à la granulométrie est proche de la valeur minimum d'une poudre quasi-sphérique.The neutral gas atomization process makes it possible to completely overcome this problem of composition. This process involves spraying a jet of liquid metal with several jets of pressurized gas. The solidification of the droplets and the cooling of the powder are carried out in a confined enclosure; the atomizing gas which fills the enclosure is neutral with respect to the atomized metal. Depending on the grade, it can be either argon or nitrogen. The device and the atomization enclosure can advantageously be designed according to the principles of the French breveis 73-43159 of December 4, 1973 or n ° 73-45788 of December 20, 1973. The powder obtained has a particle size between a few microns and 500 microns , with a spheroidal grain shape. The variable oxygen content depending on the grade is typically of the order of 100 to 200 ppm, and the specific surface area related to the particle size is close to the minimum value of a quasi-spherical powder.
Pour ces poudres sphéroïdales, la tenue mécanique des comprimés dépend de la surface de contact interparticules produite à la compaction. En pratique, on constate que pour une dureté Vickers sous 500 g supérieure à 100, la tenue mécanique et la résistance à l'effrittement des comprimés deviennent insuffisantes pour permettre une manipulation normale de ces comprimés, ce qui limite sévèrement les applications potentielles les de ces poudres pour la réalisation d'ébauches par compaction à froid.For these spheroidal powders, the mechanical strength of the tablets depends on the interparticle contact surface produced during compaction. In practice, it is found that for a Vickers hardness under 500 g greater than 100, the mechanical strength and the resistance to crumbling of the tablets become insufficient to allow normal handling of these tablets, which severely limits the potential applications of these powders for making blanks by cold compaction.
La présente invention permet à la fois de lever cette limitation sévère et d'assurer, à partir de poudre constituée de particules métalliques sphéroïdales, la réalisation de pièces de forme non fragiles présentant une dureté Vickers sous 500 g supérieure à 500.The present invention makes it possible both to overcome this severe limitation and to ensure, from powder made up of spheroidal metallic particles, the production of non-fragile shaped parts having a Vickers hardness under 500 g greater than 500.
Le principe utilisé est l'incorporation à la poudre métallique, par mélange à sec, d'un liant organique sous forme de poudre du type méthylcellulose ou plus généralement de gommes cellulosiques qui sont des polymères solubles dans l'eau. L'incorporation progressive dans le mélange d'une quantité d'eau égale à celle de méthylcellulose, c'est-à-dire de 0,2 à 2% en poids, permet la solubilisation de la méthylcellulose et évite les phénomènes de démixtion des différents constituants du mélange, tels que poudre de graphite, poudre de lubrifiant solide, etc. Le mélange est alors prêt à l'emploi et assure aux comprimés une tenue mécanique et une résistance à l'effrittement suffisante pour une manipulation normale avec des pressions de compactage de 25 à 75 daN/mm2. Ces propriétés peuvent être augmentées, si nécessaire, par un traitement d'étuvage à 120°C. L'élimination de ce liant organique est assurée au cours du frittage par un traitement thermique sous atmosphère neutre ou rédutrice comportant un palier entre 300 et 500°C, le frittage proprement dit s'effectuant sous la même atmosphère dans les conditions de temps et de température nécessitées par l'application et la nuance. Les dosages sur produit fritté indiquent une augmentation de la teneur en carbone inférieure à 0,2 fois la teneur du mélange initial en méthylcellulose et aucune variation de la teneur en oxygène par rapport à la poudre atomisée par gaz.The principle used is the incorporation into the metal powder, by dry mixing, of an organic binder in the form of a powder of the methylcellulose type or more generally of cellulose gums which are polymers soluble in water. The progressive incorporation into the mixture of an amount of water equal to that of methylcellulose, that is to say from 0.2 to 2% by weight, allows the solubilization of the methylcellulose and avoids the phenomena of demixing of the different constituents of the mixture, such as graphite powder, solid lubricant powder, etc. The mixture is then ready for use and provides the tablets with mechanical strength and sufficient crumbling resistance for normal handling with compacting pressures of 25 to 75 daN / mm 2 . These properties can be increased, if necessary, by a steaming treatment at 120 ° C. The elimination of this organic binder is ensured during sintering by a heat treatment under a neutral or reducing atmosphere comprising a plateau between 300 and 500 ° C., the actual sintering being carried out under the same atmosphere under the conditions of time and temperature required by the application and the shade. The dosages on sintered product indicate an increase in the carbon content of less than 0.2 times the content of the initial mixture in methylcellulose and no variation in the oxygen content compared to the gas atomized powder.
Ainsi, la présente invention a pour objet un procédé de fabrication de pièces de forme à partir d'un mélange de poudres de particules métalliques sphéroïdales, de lubrifiant de type stéarate et de liant organique de type gomme cellulosique, caractérisé en ce qu'on humidifie ledit mélange de poudres sèches avec de l'eau, de telle façon que le mélange pulvérulent obtenu contienne, en poids, de 0,2% à 2% de lubrifiant de type stéarate, de 0,2% à 2% de liant organique de type gomme cellulosique hydrosoluble, et entre 0,2% et 2% d'eau, et en ce qu'on soumet ledit mélange pulvérulent successivement aux deux opérations suivantes:
- a) une compaction à froid, éventuellement suivie d'un étuvage, et choisie dans le groupe de modes de compaction constitué par: la compaction unidirectionnelle en matrice, la compaction isostatique, le compactage par laminage.
- b) Un frittage en deux temps, sous atmosphère neutre ou réductrice vis à vis de la poudre compactée, le premier temps s'effectuant entre 300° et 500° C et le deuxième temps s'effectuant à une température notablement plus élevée.
- a) cold compaction, possibly followed by steaming, and chosen from the group of compaction modes consisting of: unidirectional matrix compaction, isostatic compaction, compaction by rolling.
- b) Sintering in two stages, under a neutral or reducing atmosphere with respect to the compacted powder, the first stage being carried out between 300 ° and 500 ° C and the second stage being carried out at a significantly higher temperature.
Selon l'invention, la poudre constituée de particules métalliques sphéroïdales utilisée peut avantageusement être obtenue par atomisation de métal liquide au moyen de jets gazeux.According to the invention, the powder consisting of spheroidal metal particles used can advantageously be obtained by atomization of liquid metal by means of gaseous jets.
Selon l'invention, la gomme cellulosique utilisée peut aventageusement être de la méthylcellulose.According to the invention, the cellulose gum used can advantageously be methylcellulose.
Afin de bien faire comprendre l'invention, on va décrire ci-après, à titre d'exemples non limitatifs, quatre modes de réalisation du procédé selon l'invention.In order to clearly understand the invention, four embodiments of the method according to the invention will be described below, by way of nonlimiting examples.
Réalisation, à partir d'une nuance d'acier peu allié, d'éprouvettes pour la détermination de la tenue mécanique »à vert«, à l'état brut, de compaction unidirectionelle à froid, sans la phase finale de frittage, afin de démontrer seulement l'amélioration, due à l'invention, de la résistance »à vert« des ébauches compactées à froid en vue du frittageRealization, from a low alloy steel grade, of specimens for the determination of the mechanical strength "green", in the raw state, of unidirectional cold compaction, without the final sintering phase, in order to demonstrate only the improvement, due to the invention, of the "green" resistance of the cold-compacted blanks for sintering
A partir d'une poudre atomisée par gaz, on a préparé le mélange suivant
- - 500 grammes de poudre atomisée par gaz, nuance d'acier 5 CD4 (C: au plus égal à 0,05%, Cr: 1%, Mo: 0,25%, Mn: 0,8%), granulométrie <500 micromètres dureté Vickers sous 500 g HV 0,5 = 206 ± 20,
- - 1,5 gramme de poudre de graphite,
- - 7,5 grammes de poudre de lubrifiant solid du type stéarate.
- - 500 grams of gas atomized powder, steel grade 5 CD4 (C: at most equal to 0.05%, Cr: 1%, Mo: 0.25%, Mn: 0.8%), particle size <500 Vickers hardness micrometers under 500 g HV 0.5 = 206 ± 20,
- - 1.5 grams of graphite powder,
- - 7.5 grams of solid lubricant powder of the stearate type.
Des éprouvettes parallélépipèdiques de 33 x 12 x 6 mm ont été compactées à partir de ce mélange sous 75 daN/mm2. La résistance à la rupture en flexion de ces éprouvettes, déterminée selon la norme AFNOR A 95-206, est de 0,100 daN/mm2. Cette valeur s'avère à peine suffisante pour la manipulation des comprimés. De plus, la résistance à l'effrittement des arêtes et des surfaces des comprimés est faible.Parallelepipedic specimens of 33 x 12 x 6 mm were compacted from this mixture under 75 daN / mm 2 . The flexural strength of these test pieces, determined according to AFNOR A 95-206 standard, is 0.100 daN / mm 2 . This value is barely sufficient for handling the tablets. In addition, the resistance to shattering of the edges and surfaces of the tablets is low.
Par comparaison, on a préparé un mélange à partir des constituants suivants:
- - 500 grammes de poudre atomisée par gaz, nuance d'acier 5 CD4, granulométrie <500 µm, dureté Vickers HV 0,5 = 206 ± 20,
- - 0,5 gramme de poudre de graphite,
- - 2,5 grammes de poudre de lubrifiant solide du type stéarate,
- - 5 grammes de poudre de méthylcellulose.
- - 500 grams of gas atomized powder, steel grade 5 CD4, particle size <500 µm, Vickers HV hardness 0.5 = 206 ± 20,
- - 0.5 gram of graphite powder,
- - 2.5 grams of solid lubricant powder of the stearate type,
- - 5 grams of methylcellulose powder.
On a incorporé 5 cm3 d'eau pour former un mélange humide homogène qui est conservé dans un récipient fermé.5 cm 3 of water were incorporated to form a homogeneous moist mixture which is kept in a closed container.
Les éprouvettes compactées sous 75 daN/ mm2 présentent une résistance à la rupture en flexion de 0,200 daN/mm2. Après un étuvage à 120° C, la résistance à la rupture en flexion passe à 0,400 daN/mm2. Ces valeurs autorisent une manipulation des comprimés sans précautions particulières. De plus, l'utilisation de la méthylcellulose hydrolysée comme liant de compaction apporte une amélioration spectaculaire de la résistance à l'effrittement des arêtes et des sufaces des comprimés.The test pieces compacted under 75 daN / mm 2 have a flexural breaking strength of 0.200 daN / mm 2 . After baking at 120 ° C, the flexural strength increases to 0.400 daN / mm 2 . These values allow handling of the tablets without special precautions. In addition, the use of hydrolyzed methylcellulose as a compaction binder brings a spectacular improvement in the resistance to the erosion of the edges and the sufaces of the tablets.
A partir d'une poudre atomisée par gaz de nuance 5 CD4, granulométrie <500 flm, comportant les additifs suivants en poids:
- - 0,1% de poudre de graphite,
- - 0,5% de poudre de lubrifiant solide du type stéarate,
- - 1% de poudre de méthylcellulose,
on a préparé un mélange humide dans un mélangeur industriel de capacité 200 kg par incorporation de 1% d'eau.From a powder atomized by gas of grade 5 CD4, particle size <500 μm , comprising the following additives by weight:
- - 0.1% graphite powder,
- - 0.5% solid lubricant powder of the stearate type,
- - 1% methylcellulose powder,
a wet mixture was prepared in an industrial mixer with a capacity of 200 kg by incorporating 1% of water.
La compaction de forme annulaire a été réalisée sous 40 daN/mm2 avec une presse mécanique industrielle. La densité obtenue est de 6,4 g/ cm3. Le remplissage de la poudre et l'éjection de l'ébauche ont été réalisés automatiquement au rythme de 400 pièces/heure.The annular compaction was carried out at 40 daN / mm 2 with an industrial mechanical press. The density obtained is 6.4 g / cm 3 . The filling of the powder and the ejection of the blank were carried out automatically at rhythm of 400 pieces / hour.
Ces ébauches ont pu être mises en forme par la technique du frittage-forgeage, un cycle thermique de réchauffage sous atmosphère protectrice comportant un palier entre 300 et 500°C avant le frittage proprement dit à 1150°C. Les ébauches frittées ont été densifiées par forgeage en matrice fermée suivant la technique dite du frittage-forgeage, bien connue des spécialistes. Les pièces obtenues ont la pleine densité. La teneur résiduelle en carbone après forgeage est conforme à la nuance 35 CD4, ainsi que la réponse au traitement de durcissement superficiel par carbonitruration.These blanks could be shaped by the sintering-forging technique, a thermal reheating cycle in a protective atmosphere comprising a plateau between 300 and 500 ° C before the sintering proper at 1150 ° C. The sintered blanks were densified by closed die forging according to the technique known as sintering-forging, well known to specialists. The parts obtained have full density. The residual carbon content after forging conforms to grade 35 CD4, as does the response to the surface hardening treatment by carbonitriding.
On a préparé un mélange à partir des constituants suivants:
- - 500 grammes de poudre atomisée par gaz, nuance Stellite 6, dureté Vickers HV 0,5 = 490 ± 20,
- . 2,5 grammes de poudre de lubrifiant solide du type stéarate,
- - 5 grammes de poudre de méthylcellulose.
- - 500 grams of gas atomized powder, Stellite 6 grade, Vickers HV hardness 0.5 = 490 ± 20,
- . 2.5 grams of solid lubricant powder of the stearate type,
- - 5 grams of methylcellulose powder.
On a incorporé 5 cm3 d'eau pour former un mélange humide homogène qui est conservé dans un récipient fermé.5 cm 3 of water were incorporated to form a homogeneous moist mixture which is kept in a closed container.
Des échantillons sous forme de plaquettes des 33 x 12 x 4 mm et de bagues de diamètre extérieur20 mm, de diamètre intérieur 12 mm, de hauteur 12 mm, ont été compactés sous des pressions variant de 25 daN/mm2 à 75 daN/mm2. Bien que la densité relative de ces échantillons soit peu différente de la densité relative de la poudre tassée, leur manipulation peut être effectuée sans précautions particulières.Samples in the form of plates of 33 x 12 x 4 mm and rings of outside diameter 20 mm, inside diameter 12 mm, height 12 mm, were compacted under pressures varying from 25 daN / mm 2 to 75 daN / mm 2 . Although the relative density of these samples is little different from the relative density of the packed powder, their handling can be carried out without special precautions.
Par comparaison, les comprimés réalisés à partir de mélanges sans méthylcellulose hydrolysée sont très friables et ne peuvent être manipulés, même après une compression sous 150 daN/mm2. Une densification pratiquement complète de ces comprimés a pu être obtenue par un traitement thermique sous vide comportant un palier entre 300 et 500°C et un frittage à température élevée dépendant de la structure à obtenir, cette température pouvant se situer dans certains cas entre 1250°C et 1350°C, par exemple.By comparison, the tablets produced from mixtures without hydrolyzed methylcellulose are very friable and cannot be handled, even after compression under 150 daN / mm 2 . A practically complete densification of these tablets could be obtained by a heat treatment under vacuum comprising a plateau between 300 and 500 ° C. and a sintering at high temperature depending on the structure to be obtained, this temperature being able in some cases to be between 1250 ° C and 1350 ° C, for example.
A partir du même mélange que celui indiqué dans l'exemple 3, on a réalisé des ébauches sphériques par compaction isostatique à froid. La poudre est placée dans des moules de forme en latex et les moules placés dans une enceinte où est appliquée une pression hydraulique de 2000 à 3500 bans. On a obtenu ainsi des billes de 8 à 30 mm de diamètre qui ont été frittées dans les conditions indiquées dans l'exemple 3.From the same mixture as that indicated in Example 3, spherical blanks were produced by cold isostatic compaction. The powder is placed in latex molds and the molds placed in an enclosure where a hydraulic pressure of 2,000 to 3,500 bans is applied. Beads 8 to 30 mm in diameter were thus obtained which were sintered under the conditions indicated in Example 3.
A partir d'une poudre atomisée par gaz, nuance d'acier 316 L, granulométrie 100 à 250 ¡.tm, comportant 1% en poids de méthylcellulose, on a incorporé 1% d'eau par passage dans un mélangeur continu. Le mélange humide est alimenté en continu dans l'entre-cylindre d'un laminoir duo muni de cylindres de 370 mm de diamètre et de 300 mm de largeur de table avec leurs axes de rotation respectifs disposés dans un même plan horizontal. Une bande cohérente de largeur 300 mm, épaisseur 1 mm, densité 6,50 g/cm3, a été produite à 0,5 m/minute. Après compaction par laminage, la bande passe à le même vitesse dans un four à passage sous atmosphère d'ammoniac craqué comportant une zone à 300-500° C où s'élimine le liant organique et une zone à 1150°C où s'effectue le frittage proprement dit. Gette bande conserve une porosité de 25% en volume et peut être utilisée, par exemple, comme milieu filtrant.From a gas atomized powder, steel grade 316 L, particle size 100 to 250 µm, comprising 1% by weight of methylcellulose, 1% of water was incorporated by passage through a continuous mixer. The wet mixture is fed continuously into the inter-cylinder of a duo rolling mill provided with cylinders of 370 mm in diameter and 300 mm in table width with their respective axes of rotation arranged in the same horizontal plane. A coherent strip 300 mm wide, 1 mm thick, density 6.50 g / cm 3 , was produced at 0.5 m / minute. After compaction by rolling, the strip passes at the same speed in a passage oven under a cracked ammonia atmosphere comprising a zone at 300-500 ° C where the organic binder is eliminated and a zone at 1150 ° C where is carried out the actual sintering. This strip retains a porosity of 25% by volume and can be used, for example, as a filter medium.
Claims (3)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7928066A FR2469233B1 (en) | 1979-11-14 | 1979-11-14 | |
FR7928066 | 1979-11-14 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0029389A1 EP0029389A1 (en) | 1981-05-27 |
EP0029389B1 true EP0029389B1 (en) | 1984-03-14 |
Family
ID=9231666
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP80401633A Expired EP0029389B1 (en) | 1979-11-14 | 1980-11-14 | Process for producing shaped articles from spherical metal-particle powders |
Country Status (4)
Country | Link |
---|---|
US (1) | US4391772A (en) |
EP (1) | EP0029389B1 (en) |
DE (1) | DE3067034D1 (en) |
FR (1) | FR2469233B1 (en) |
Families Citing this family (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58141306A (en) | 1982-02-12 | 1983-08-22 | Sumitomo Metal Ind Ltd | Spraying medium for producing metallic powder |
SE438275B (en) * | 1983-09-09 | 1985-04-15 | Hoeganaes Ab | MIX-FREE IRON-BASED POWDER MIX |
JPS60221506A (en) * | 1984-04-17 | 1985-11-06 | Honda Motor Co Ltd | Formation of sliding surface in machine tool |
US4721599A (en) * | 1985-04-26 | 1988-01-26 | Hitachi Metals, Ltd. | Method for producing metal or alloy articles |
US4587096A (en) * | 1985-05-23 | 1986-05-06 | Inco Alloys International, Inc. | Canless method for hot working gas atomized powders |
US4624706A (en) * | 1985-07-02 | 1986-11-25 | Inco Alloys International, Inc. | Weld wire from extruded nickel containing powder |
US4591482A (en) * | 1985-08-29 | 1986-05-27 | Gorham International, Inc. | Pressure assisted sinter process |
JPS6274001A (en) * | 1985-09-26 | 1987-04-04 | Nippon Kokan Kk <Nkk> | Manufacture of sintered metallic body |
US4830994A (en) * | 1986-03-31 | 1989-05-16 | The Dow Chemical Company | Greenware binder |
GB8621712D0 (en) * | 1986-09-09 | 1986-10-15 | Mixalloy Ltd | Flat products |
US4722826A (en) * | 1986-09-15 | 1988-02-02 | Inco Alloys International, Inc. | Production of water atomized powder metallurgy products |
US4955798B1 (en) * | 1988-10-28 | 1999-03-30 | Nuova Merisinter S P A | Process for pretreating metal powder in preparation for compacting operations |
GB9102290D0 (en) * | 1991-02-02 | 1991-03-20 | Mixalloy Ltd | Production of flat products |
FR2707191B1 (en) * | 1993-07-06 | 1995-09-01 | Valinox | Metallic powder for making parts by compression and sintering and process for obtaining this powder. |
US5665014A (en) * | 1993-11-02 | 1997-09-09 | Sanford; Robert A. | Metal golf club head and method of manufacture |
EP0913220B1 (en) | 1997-03-19 | 2008-12-10 | JFE Steel Corporation | Iron base powder mixture for powder metallurgy excellent in fluidity and moldability |
SE511834C2 (en) * | 1998-01-13 | 1999-12-06 | Valtubes Sa | Fully dense products made by uniaxial high speed metal powder pressing |
DE10014403A1 (en) * | 2000-03-24 | 2001-09-27 | Wolfgang Kochanek | Process for the powder metallurgy production of metal bodies comprises mixing a metal compound powder such as oxide powder with a rheology-improving additive, removing the additive; and reducing the metal compound using a reducing gas |
CA2534472A1 (en) * | 2003-09-03 | 2005-03-17 | Apex Advanced Technologies, Llc | Composition for powder metallurgy |
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BE517440A (en) * | ||||
US2598796A (en) * | 1947-02-08 | 1952-06-03 | Husqvarna Vapenfabriks Ab | Methods for the reduction and sintering of bodies containing reducible metal compounds |
US3725142A (en) * | 1971-08-23 | 1973-04-03 | Smith A Inland Inc | Atomized steel powder having improved hardenability |
GB1452510A (en) * | 1973-01-05 | 1976-10-13 | Xerox Corp | Spheroidization method and apparatus |
US3988524A (en) * | 1973-01-15 | 1976-10-26 | Cabot Corporation | Powder metallurgy compacts and products of high performance alloys |
US3989518A (en) * | 1975-05-08 | 1976-11-02 | United States Steel Corporation | Production of powder metallurgical parts by formation of sintered preforms in thermally degradable molds |
CA1119847A (en) * | 1977-09-26 | 1982-03-16 | Minnesota Mining And Manufacturing Company | Infiltrated molded articles of spherical non-refractory metal powders |
US4298383A (en) * | 1979-06-25 | 1981-11-03 | National-Standard Company | Low viscosity composition for forming shaped bodies |
-
1979
- 1979-11-14 FR FR7928066A patent/FR2469233B1/fr not_active Expired
-
1980
- 1980-10-31 US US06/202,825 patent/US4391772A/en not_active Expired - Lifetime
- 1980-11-14 EP EP80401633A patent/EP0029389B1/en not_active Expired
- 1980-11-14 DE DE8080401633T patent/DE3067034D1/en not_active Expired
Non-Patent Citations (1)
Title |
---|
Pulvermetallurgie Sinter- und Verbundwerkstoffe Seite 342-343 * |
Also Published As
Publication number | Publication date |
---|---|
DE3067034D1 (en) | 1984-04-19 |
US4391772A (en) | 1983-07-05 |
FR2469233B1 (en) | 1982-06-18 |
FR2469233A1 (en) | 1981-05-22 |
EP0029389A1 (en) | 1981-05-27 |
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