EP2552630B1 - Method for producing shaped bodies from aluminium alloys - Google Patents

Method for producing shaped bodies from aluminium alloys Download PDF

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Publication number
EP2552630B1
EP2552630B1 EP11720714.2A EP11720714A EP2552630B1 EP 2552630 B1 EP2552630 B1 EP 2552630B1 EP 11720714 A EP11720714 A EP 11720714A EP 2552630 B1 EP2552630 B1 EP 2552630B1
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EP
European Patent Office
Prior art keywords
binder
debinding
aluminum
thermal debinding
carried out
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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EP11720714.2A
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German (de)
French (fr)
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EP2552630A1 (en
Inventor
Herbert Danninger
Christian Gierl
Branislav Zlatkov
Johan Ter Maat
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Technische Universitaet Wien
Rupert Fertinger GmbH
BASF SE
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Technische Universitaet Wien
Rupert Fertinger GmbH
BASF SE
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Priority to PL11720714T priority Critical patent/PL2552630T3/en
Publication of EP2552630A1 publication Critical patent/EP2552630A1/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F3/00Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
    • B22F3/22Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces for producing castings from a slip
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F3/00Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
    • B22F3/20Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces by extruding
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F3/00Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
    • B22F3/12Both compacting and sintering
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F3/00Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
    • B22F3/10Sintering only
    • B22F3/1017Multiple heating or additional steps
    • B22F3/1021Removal of binder or filler
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F3/00Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
    • B22F3/10Sintering only
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F3/00Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
    • B22F3/22Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces for producing castings from a slip
    • B22F3/225Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces for producing castings from a slip by injection molding
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F3/00Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
    • B22F3/24After-treatment of workpieces or articles
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C1/00Making non-ferrous alloys
    • C22C1/04Making non-ferrous alloys by powder metallurgy
    • C22C1/0408Light metal alloys
    • C22C1/0416Aluminium-based alloys
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C21/00Alloys based on aluminium
    • C22C21/06Alloys based on aluminium with magnesium as the next major constituent

Definitions

  • a feedstock is prepared in the form of a sprayable granulate of metal powder and a plastic component comprising at least two intensively mixed polymer components.
  • This feedstock is then sprayed into molded parts in plastic injection molding machines.
  • This so-called “green body” or “green body” usually contains about 40% by volume of plastic binder, which is removed in the subsequent step, the so-called debindering, for the most part. There remains only a residual component of the binder, the so-called. "Backbone”, which ensures the residual strength of the unbent body.
  • Debinding can be done in a variety of ways, e.g.
  • EP 329,475 A2 describes the processing of various metal powders, ceramics or alloys into moldings using a special organic binder mixture.
  • Aluminum is mentioned as one of many possible starting materials, which should be sinterable with the binder system there.
  • Suitable atmospheres for debinding include oxidizing, reducing and inert atmospheres - under low, normal or overpressure - and thus all conceivable options.
  • Carbides were also found in the sintered bodies, the presence of which is attributed to contamination with carbon from the furnace, but which is much more likely to result from incomplete debindering and hence the logical presence of organic carbon in the brown compact. Consequently, it is stated that debinding should be done in a vacuum and not in air.
  • a particular difficulty in the processing of aluminum in the manner described above is also the relatively low melting point of aluminum (660 ° C) produced by the addition of alloying elements, e.g. Tin, still lowered.
  • alloying elements e.g. Tin
  • the resulting problem is that the debinding of the plastic component must be completed at very low temperatures, which often makes the available process window too small to ensure complete removal.
  • undesirable reactions of residual organic constituents with the metallic components can occur, hindering sintering and thus impairing the mechanical properties that can be achieved.
  • the object of the invention was, in this context, the development of a metal powder injection molding process, by the moldings of aluminum materials with good mechanical properties can be produced in a simpler and reproducible manner.
  • the aluminum alloy contains, besides aluminum, one or more other metals which are not specifically limited.
  • the alloying partners are selected from the group consisting of magnesium, copper, silicon and manganese, and are more preferably contained in a respective proportion of 0.5 to 25% by weight to obtain molded articles having desirable properties.
  • Significantly lower melting metals, such as bismuth, tin, lead, indium, or even zinc, or alloys such as Wood's metal, sometimes called sintering aids for lowering serve the temperature of the onset of melting, are not required according to the present invention, but can still be added as alloying partners, if desired, to obtain sintered bodies of the corresponding alloys.
  • the other metals are used as alloys with aluminum, ie as master alloy or so-called master alloy powder.
  • binders which are known to be removable at low temperatures, more preferably polyacetal-based binders, for example polyoxymethylene (POM) binders, for example those described by BASF in US Pat EP 413,231 .
  • POM polyoxymethylene
  • WO 94/25205 and especially EP 446,708 disclosed and sold under the brand name Catamold ® In order to promote rapid and complete removability at low temperatures and in the presence of oxygen, a high polyacetal content is desirable in the binder, and therefore, the binder is preferably 50 to 95%, more preferably 80 to 90%, of polyacetal.
  • binder systems can be used which are based on wax polymer-based and in which the main component wax by previous Wegsentbind réelle, ie prior to the inventive implementation of the thermal debinding in the presence of oxygen, is removed.
  • Debinding in step c) of the process of the invention may involve a single step of thermal debinding in the presence of oxygen, in which the entire binder is removed.
  • one or more preceding debinding steps may be performed to remove the bulk of the binder, followed by the thermal debinding step of the present invention to remove the residual binder in the presence of oxygen.
  • a previous debinding step may also be a thermal debindering - in the absence or also in the presence of oxygen. That is, as debindering can also be a multi-stage thermal debindering at different process parameters, such as different temperature or atmosphere, eg without and with oxygen or with air and pure oxygen, etc.
  • the bulk of the binder is already removed from the composition, so that in the subsequent thermal debinding preferably only the "backbone" component needs to be removed.
  • the catalytic debinding is carried out preferably in the presence of at least one acid selected from nitric acid, oxalic acid, formic acid and acetic acid, since these acids accelerate the complete removal of the preferred polyacetal binder by acidolysis, without leading to undesirable side reactions with the alloying partners.
  • the bulk of the binder is obtained by extraction with a suitable solvent or solvent mixture, e.g. Acetone, n-heptane, water etc., removed.
  • a catalytic debindering with sublimed oxalic acid is particularly preferred according to the present invention.
  • the thermal debinding to remove the residual binder in step c) is carried out at a relatively low temperature in order to suppress oxidation reactions, especially of the aluminum in the powder mixture.
  • a relatively low temperature herein is meant a temperature well below the melting point of aluminum, preferably below 500 ° C, more preferably between 100 and 420 ° C.
  • an empirically optimized temperature profile for the respective powder mixture is set, which preferably provides a heating rate of not more than 5 K / min, more preferably not more than 1 to 2 K / min.
  • the sintering step d) of the process of the present invention is not specifically limited except for the requirement that the binder must be completely removed beforehand. Preferably, however, is sintered to form a liquid phase, as will be explained in more detail below.
  • Embodiments according to the invention are therefore preferred in which the completely debinded browning material is sintered in step d) to form a liquid phase.
  • This liquid phase which in the view of the inventors - without wishing to be bound to a particular theory - to a part intermediary, but predominantly stationary, ie in thermodynamic equilibrium with the solid Al phase, is present over microcracks, pores or the like "Openings" in the oxide skins of the metal powder particles and infiltration of the oxide skins forth the required contact between the metals in the powder mixture ago and thus supports the formation of a high-density sintered body from the completely unbonded B Hurnling.
  • the sintering in step d) is carried out at a temperature between the solidus and the liquidus temperature of the respective aluminum alloy, so that at any time during the sintering process only a controllable by the choice of a corresponding temperature profile proportion of the alloy metals in liquid Phase exists, which effectively prevents loss of dimensional and dimensional stability.
  • the composition of the particular atmosphere in the individual steps of the process according to the invention is not particularly limited except for the presence of the oxygen in the thermal debinding in step c), and the person skilled in the art can select in each individual step the most suitable atmosphere for the respective powder mixture , whereby also vacuum is possible.
  • the sintering step d) is preferably carried out in an extremely dry nitrogen-containing atmosphere, i. in pure nitrogen, under normal pressure or reduced pressure ("partial pressure sintering"), or in a mixture of nitrogen and pure inert gas (helium, argon), preferably with a dew point ⁇ -40 ° C, since the presence of nitrogen with the wettability of the powder the resulting molten metal significantly supported.
  • sintering may be followed by a suitable after-treatment, by means of which the finished molded parts are obtained in the desired shape.
  • a suitable after-treatment for example, the known method of hot isostatic pressing (HIP) can be used to bring the moldings to the desired final density.
  • HIP hot isostatic pressing
  • residual pores remaining after sintering are pressed by the simultaneous action of external gas pressure and temperature, and the pore walls are welded together.
  • feedstocks prepared in the examples below were homogenized in a heated kneader at 190 ° C. From these feedstocks, tensile test bars or hollow cylinders were molded by means of injection molding in accordance with ISO 2740, the method according to the invention being used as follows. To produce the green parts, a hydraulic injection molding machine (Battenfeld HM 600/130) with PIM equipment was used.
  • the feedstock was first filled into a funnel of the injection molding machine.
  • the powder injection molding for the production of the green parts was carried out in the following steps:
  • the prepared feed material was plasticized and pre-dosed by means of a heated injection cylinder in which a screw rotates according to preset setting parameters (such as, for example, rotational speed, metering volume, dynamic pressure, etc.).
  • preset setting parameters such as, for example, rotational speed, metering volume, dynamic pressure, etc.
  • the pre-dosed quantity was injected into a suitably tempered tool.
  • the plasticizing temperature in the injection cylinder was between 120 and 220 ° C, while in the tool between 25 and 140 ° C prevailed.
  • the injection mold was opened and the green part ejected from the tool and removed with a handling.
  • Example 1 Tension rods: Solution debonding / thermal debinding
  • a commercially available metal powder mixture (Alumix ® 231 of Ecka) consisting of aluminum, with 14 wt .-% of silicon, 2.5 wt .-% copper and 0.6 wt .-% magnesium, was with a group consisting of wax / thermoplastic Solvent binder carefully mixed into a feedstock.
  • Feedstock component Proportion (% by weight)
  • Solvent binder wax content 14.8
  • Solvent binder thermoplastic content 8.2 stearic acid 2.2 100.0 *
  • This feedstock was first debinded by solvent extraction in a 60 L oven with acetone at a temperature of 45 ° C over 12 h.
  • the Bhoffnling thus obtained contained a residual binder content of about 14.5 wt .-%, which then by thermal debinding according to the invention by means of a temperature profile of 150 ° C to 320 ° C for 1 h and then from 320 to 420 ° C for 1.5 h was removed at a heating rate of 3 K / min under a pure oxygen-containing atmosphere.
  • the thus completely unbonded B syndromenling was then sintered at 560 ° C within 1 h in pure nitrogen (dew point: -50 ° C).
  • Example 2 Tension rods: thermal debindering in one step
  • Feedstock component Proportion (% by weight) aluminum powder 67.1 Master Alloy Powder * 4.3 POM Binder 25.8
  • PMMA polymethylmethacrylate
  • the sintering was carried out at a furnace setting temperature of 665 ° C, which corresponds to a temperature within the furnace of about 630 ° C, during 1 h in pure nitrogen.
  • a first thermal debinding was carried out in a 50 l oven in 500 l / h of air at 180 ° C for 14 h. Weight loss: 27.0%.
  • Example 3 a thermal debindering to 420 ° C under pure oxygen within 1 h, after which it was again sintered at a Ofeneinstelltemperatur of 665 ° C for 1 h under nitrogen.
  • Example 4 a catalytic debinding was carried out analogously to Example 4, but using 80 g of anhydrous oxalic acid on a Sublimierschale instead of HNO 3 at 140 ° C for 24 h. Weight loss: 23.0%. Due to the use of oxalic acid, no outgrowths appeared on the surface. Subsequently, thermal debinding and sintering were also carried out analogously to Example 4.
  • Feedstock component Proportion (% by weight) Alumix 231 powder * 70.8 POM Binder * 25.6 surfactant ** 3.6 100.0 * Commercially available metal powder mixture of aluminum with 14% by weight of silicon, 2.5% by weight of copper and 0.6% by weight of magnesium (from Ecka) ** Ethoxylated C 13 -C 15 oxo alcohol with 7 EO units
  • Example 5 a catalytic debinding was carried out analogously to Example 5. Weight loss: 25.2%. Subsequently, thermal debinding and sintering were carried out analogously to Example 4, but at a Ofeneinstelltemperatur of 560 ° C.
  • Feedstock component Proportion (% by weight) aluminum powder 68.0 Master Alloy Powder * 4.3 POM Binder 24.0 surfactant ** 3.7 100.0 * Master alloy of aluminum and magnesium in the ratio 50:50 ** Ethoxylated C 13 -C 15 oxo alcohol with 7 EO units
  • Example 5 a catalytic Entbindtation analogous to Example 5. Weight loss: 23.2%. Subsequently, thermal debinding and sintering were carried out analogously to Example 4.
  • Example 8 Hollow Cylinder: Catalytic / Thermal Debinding
  • Feedstock component Proportion (% by weight) aluminum powder 68.0 Master Alloy Powder * 4.3 POM Binder 24.0 surfactant ** 3.7 100.0 * Master alloy of aluminum and magnesium in the ratio 50:50 ** Ethoxylated C 13 -C 15 oxo alcohol with 7 EO units
  • Example 5 a catalytic debinding was carried out analogously to Example 5. Weight loss: 23.7%. Subsequently, thermal debinding and sintering were carried out analogously to Example 4.
  • Example 5 a catalytic debinding analogous to Example 5. Weight loss: 25.7%. Subsequently, thermal debinding and sintering were carried out analogously to Example 4.
  • Example 10 Hollow Cylinder: Catalytic / Thermal Debinding
  • Feedstock component Proportion (% by weight) aluminum powder 67.1 Master Alloy Powder * 4.3 POM Binder 25.8
  • PMMA polymethylmethacrylate
  • Example 5 a catalytic debinding analogous to Example 5. Weight loss: 25.6%. Subsequently, thermal debinding and sintering were carried out analogously to Example 4.
  • sintered bodies of aluminum alloys can be provided by means of injection molding, which are suitable for practical use in many fields, e.g. in the transport sector, construction, mechanical engineering, packaging, iron and steel, electrical engineering, household appliances, etc., for example for heat dissipation in electronic devices ("heat sinks") or as components of air conditioning systems.

Description

Die Technologie des Metallpulverspritzgusses hat in den letzten Jahren einen enormen Aufschwung genommen und ist zur Herstellung von kompliziert geformten Kleinteilen eine eingeführte Technologie mit einem weltweiten Jahresumsatz von etwa 1 Mrd. €. Die Möglichkeit, die Formgebungstechnologie des Kunststoffspritzgusses mit der Werkstoffvielfalt der Pulvertechnologie zu verbinden, hat für viele Werkstoffe interessante Märkte erschlossen.The technology of metal powder injection molding has gained a tremendous boost in recent years and is an established technology with a global annual turnover of about € 1 billion for the production of intricately shaped small parts. The possibility of combining the molding technology of plastic injection molding with the material diversity of powder technology has opened up interesting markets for many materials.

Das Herstellungsverfahren besteht im Wesentlichen aus den nachstehend beschriebenen Prozessschritten. Zunächst wird ein Feedstock in Form eines spritzbaren Granulats aus Metallpulver und einer Kunststoffkomponente, die zumindest zwei intensiv vermischte Polymerkomponenten umfasst, hergestellt. Dieser Feedstock wird anschließend in Kunststoffspritzgussmaschinen zu Formteilen verspritzt. Dieser sog. "Grünkörper" oder "Grünling" enthält üblicherweise ca. 40 Vol.-% Kunststoffbinder, der im nachfolgenden Schritt, der sog. Entbinderung, zum überwiegenden Teil entfernt wird. Es verbleibt nur eine Restkomponente des Binders, das sog. "Backbone", das die Restfestigkeit des entbinderten Körpers gewährleistet. Die Entbinderung kann auf vielfältige Weise geschehen, z.B. thermisch, durch Lösungsmittel, katalytisch usw., wobei sie sehr gut auf den eingesetzten Kunststoffbinder abgestimmt sein muss. Der entbinderte Körper, der sog. "Braunteil" oder "Bräunling", wird nun einem Sinterprozess unterzogen, in dessen erster Stufe normalerweise der "Backbone"-Restbinder thermisch entfernt und der Körper dann unter entsprechender Schrumpfung zu einem annähernd dichten metallischen Bauteil gesintert wird. Die Technologie wird derzeit für hoch- und niedriglegierte Stähle, Edelmetalle, Hartmetalle, aber auch für Keramiken eingesetzt.The manufacturing process consists essentially of the process steps described below. First, a feedstock is prepared in the form of a sprayable granulate of metal powder and a plastic component comprising at least two intensively mixed polymer components. This feedstock is then sprayed into molded parts in plastic injection molding machines. This so-called "green body" or "green body" usually contains about 40% by volume of plastic binder, which is removed in the subsequent step, the so-called debindering, for the most part. There remains only a residual component of the binder, the so-called. "Backbone", which ensures the residual strength of the unbent body. Debinding can be done in a variety of ways, e.g. thermally, by solvent, catalytically, etc., where it must be very well matched to the plastic binder used. The debinded body, the so-called "brown part" or "browning", is now subjected to a sintering process, in the first stage of which the "backbone" residual binder is normally thermally removed and the body is then sintered with appropriate shrinkage to form an approximately dense metallic component. The technology is currently used for high and low alloy steels, precious metals, hard metals, but also for ceramics.

Obwohl mehrere diesbezügliche Patente existieren, wurde Metallpulverspritzguss für Aluminiumwerkstoffe bisher noch nicht erfolgreich industriell eingeführt, da sich die Mechanismen des Sinterns von Aluminiumlegierungen sehr stark von dem der oben erwähnten Werkstoffe unterscheiden. Die Anwesenheit von nicht reduzierbaren Oxiden auf der Oberfläche von Aluminiumpulvern behindert nämlich massiv die Sinterung. Aus diesem Grund wird in der Fachliteratur auch durchwegs eine sauerstofffreie Atmosphäre beschrieben oder deren Verwendung nahe gelegt.Although several related patents exist, metal powder injection molding for aluminum materials has not been successfully introduced industrially since the mechanisms of sintering aluminum alloys are very different from those of the above-mentioned materials. The presence of non-reducible oxides on the surface of aluminum powders massively hinders sintering. For this reason, an oxygen-free atmosphere is generally described or suggested to be used in the specialist literature.

EP 329.475 A2 beschreibt die Verarbeitung diverser Metallpulver, Keramiken bzw. Legierungen zu Formkörpern unter Verwendung eines speziellen organischen Bindergemischs. Aluminium wird dabei als eines von zahlreichen möglichen Ausgangsmaterialien genannt, die mit dem dortigen Bindersystem sinterbar sein sollen. Als in Frage kommende Atmosphären zum Entbindern werden oxidierende, reduzierende und inerte Atmosphären - unter Unter-, Normal- oder Überdruck - und somit alle nur denkbaren Optionen genannt. EP 329,475 A2 describes the processing of various metal powders, ceramics or alloys into moldings using a special organic binder mixture. Aluminum is mentioned as one of many possible starting materials, which should be sinterable with the binder system there. Suitable atmospheres for debinding include oxidizing, reducing and inert atmospheres - under low, normal or overpressure - and thus all conceivable options.

Katou et al., J. Jpn. Soc. Powder and Powder Metall. 42(9), 1068-72 (1995 ), offenbaren die Herstellung von Ti-Al-Legierungen in Verhältnissen von 45:55 bis 55:45, wobei in Luft oder Ar-Vakuum entbindert wurde. Das Ziel war eine Entbinderung über 90 %. Die angestrebten Sinterdichten von über 95 % werden dabei nur zum Teil erreicht - auch beim Sintern im Ar-Vakuum, wo die Dichte jedoch durchwegs höher war als nach Entbinderung in Luft, was auf Oxidation zurückgeführt wird, die beim Entbindern in Luft durchwegs stärker ausgeprägt war als in Ar-Vakuum. In den Sinterkörpern wurden zudem Carbide festgestellt, deren Gegenwart auf eine Kontamination mit Kohlenstoff aus dem Ofen zurückgeführt wird, die aber wohl viel eher aus der unvollständigen Entbinderung und der daher logischen Gegenwart von organischem Kohlenstoff im Bräunling resultiert. Folglich wird festgestellt, dass die Entbinderung im Vakuum und nicht in Luft erfolgen sollte. Katou et al., J. Jpn. Soc. Powder and Powder Metal. 42 (9), 1068-72 (1995 ) disclose the preparation of Ti-Al alloys in proportions of 45:55 to 55:45, while debinding in air or Ar vacuum. The goal was a debindering over 90%. The targeted sintering densities of more than 95% are achieved only partially - even when sintered in Ar vacuum, where the density was consistently higher than after debindering in air, which is attributed to oxidation, which was consistently pronounced when debinding in air as in Ar-vacuum. Carbides were also found in the sintered bodies, the presence of which is attributed to contamination with carbon from the furnace, but which is much more likely to result from incomplete debindering and hence the logical presence of organic carbon in the brown compact. Consequently, it is stated that debinding should be done in a vacuum and not in air.

In J. Jpn. Soc. Powder and Powder Metall. 51(7), 2004-7 (2004 ), offenbaren K. Katou et al. einige Jahre später die Verarbeitung von Rein-Aluminium zu Sinterkörpern mittels MIM, wobei zur Untersuchung des Einflusses der Atmosphäre beim Entbindern auf die Dichte der Sinterkörper sowohl bei 325 °C in Luft als auch bei 380 °C unter Argon-Überdruck entbindert wurde, allerdings in allen Fällen ganz gezielt nur zu "ca. 90%". Nach Entbinderung in Argon betrug die Dichte der erhaltenen Sinterkörper, je nach Körngröße, 86, 89 bzw. 96 %, während sie bei Luft-Entbinderung in zwei Fällen auf ca. 65 % und im dritten Fall, unter Verwendung des feinkörnigsten Ausgangspulvers, auf 86 % abfiel. Als Gründe dafür werden Oxidation des Aluminiums bzw. die Menge an Restbinder angegeben. So erhöhte sich der Sauerstoffgehalt beim Entbindern in Ar um 50 %, während er in Luft auf das 2- bis 3fache zunahm. Der Kohlenstoff-Gehalt betrug im Luft-entbinderten Sinterkörper sogar das 5fache jenes in Ar. Weiters wird festgestellt, dass die Untersuchungen der thermischen Zersetzung des organischen Binders bis zu einer Temperatur von 500 °C gezeigt hätten, dass in Inertgas eine Zersetzungsrate von 99,5 %, in Luftatmosphäre jedoch nur eine Zersetzungsrate von 96,5 % erzielt werden könne und dass die bei Luft-Entbinderung erzielten Dichten unter 90 % nicht ausreichend seien. Durch Sintern nahe dem Schmelzpunkt von Aluminium sei es zudem zu unerwünschtem teilweisem Schmelzen der Proben gekommen, was als Gefahr bezeichnet wird, weswegen die Sintertemperatur zu senken sei.In J. Jpn. Soc. Powder and Powder Metal. 51 (7), 2004-7 (2004 ), K. Katou et al. a few years later, the processing of pure aluminum to sintered bodies by means of MIM, wherein to investigate the influence of the atmosphere during debindering on the density of the sintered body was debindered both at 325 ° C in air and at 380 ° C under argon pressure, but in in all cases specifically only to "about 90%". After debindering in argon, the density of the resulting sintered bodies, depending on the grain size, was 86, 89 and 96% respectively, whereas in air debindering in two cases it was about 65% and in the third case, using the finest-grained starting powder. fell to 86%. The reasons given for this are oxidation of the aluminum or the amount of residual binder. Thus, the oxygen content of binder removal in Ar increased by 50%, while in air it increased by 2 to 3 times. The carbon content in the air-debindered sintered body was even 5 times that in Ar. Furthermore, it is found that the investigations of the thermal decomposition of the organic binder up to a temperature of 500 ° C would have shown that in inert gas, a decomposition rate of 99.5%, in the air atmosphere, however, only a decomposition rate of 96.5% can be achieved, and that the densities achieved with air-debindering are below 90% insufficient. By sintering close to the melting point of aluminum, it had also come to undesirable partial melting of the samples, which is referred to as a danger, which is why the sintering temperature should be lowered.

Eine besondere Schwierigkeit bei der Verarbeitung von Aluminium auf die oben beschriebene Weise ist auch der relativ niedrige Schmelzpunkt von Aluminium (660 °C), der durch den Zusatz von Legierungselementen, wie z.B. Zinn, noch gesenkt wird. Das daraus resultierende Problem besteht darin, dass die Entbinderung der Kunststoffkomponente bei sehr niedrigen Temperaturen abgeschlossen sein muss, wodurch das zur Verfügung stehende Prozessfenster oftmals zu klein wird, um eine vollständige Entfernung zu gewährleisten. Falls dies jedoch nicht gelingt, kann es zu unerwünschten Reaktionen von organischen Restbestandteilen mit den metallischen Komponenten kommen, die die Sinterung behindern und damit die erzielbaren mechanischen Eigenschaften verschlechtern.A particular difficulty in the processing of aluminum in the manner described above is also the relatively low melting point of aluminum (660 ° C) produced by the addition of alloying elements, e.g. Tin, still lowered. The resulting problem is that the debinding of the plastic component must be completed at very low temperatures, which often makes the available process window too small to ensure complete removal. However, if this fails, undesirable reactions of residual organic constituents with the metallic components can occur, hindering sintering and thus impairing the mechanical properties that can be achieved.

Beispielsweise beschreiben Liu et al. in Powder Metallurgy 51, 78-83 (2008 ) ein Verfahren unter Zusatz von Zinn als Legierungsmetall sowie von Magnesiumblöcken, wobei das Magnesium als "Opfermetall", d.h. als Sauerstoff- und Feuchtigkeitsfänger, dient.For example, describe Liu et al. in Powder Metallurgy 51, 78-83 (2008 ) a method with the addition of tin as alloying metal as well as magnesium blocks, wherein the magnesium as a "sacrificial metal", ie as an oxygen and moisture scavenger used.

Ziel der Erfindung war vor diesem Hintergrund die Entwicklung eines Metallpulverspritzgussverfahrens, durch das Formkörper aus Aluminiumwerkstoffen mit guten mechanischen Eigenschaften auf einfachere Weise und reproduzierbar hergestellt werden können.The object of the invention was, in this context, the development of a metal powder injection molding process, by the moldings of aluminum materials with good mechanical properties can be produced in a simpler and reproducible manner.

OFFENBARUNG DER ERFINDUNGDISCLOSURE OF THE INVENTION

Dieses Ziel haben die Erfinder durch Bereitstellung eines Verfahrens zur Herstellung von Formkörpern auf Basis von Aluminiumlegierungen durch Metallpulverspritzguss erreicht, das die folgenden Schritte umfasst:

  1. a) Herstellung eines Feedstocks durch Vermischen der in der gewünschten Legierung enthaltenen Metalle in Form von Metallpulvern und/oder einem oder mehreren Metalllegierungspulvern mit einem Binder;
  2. b) Herstellung eines Grünlings durch Spritzgießen des Feedstocks;
  3. c) Herstellung eines Bräunlings durch zumindest teilweises Entfernen des Binders aus dem Grünling durch katalytisches und/oder Lösungsmittel- und/oder thermisches Entbindern;
  4. d) Sintern des zumindest teilweise entbinderten Bräunlings zum Erhalt des gewünschten Formkörpers;
wobei das erfindungsgemäße Verfahren dadurch gekennzeichnet ist, dass in Schritt c) der Binder vollständig entfernt wird, wobei, gegebenenfalls nach Durchführung eines oder mehrerer vorhergehender Entbinderungsstufen, eine thermische Entbinderung zur Entfernung des (Rest-)Binders erfolgt, die in einer zumindest 0,5 Vol.-% Sauerstoff enthaltenden Atmosphäre durchgeführt wird, wonach der so erhaltene, vollständig entbinderte Bräunling gesintert wird.This object has been achieved by the inventors by providing a process for the production of moldings based on aluminum alloys by metal injection molding, comprising the following steps:
  1. a) production of a feedstock by mixing the metals contained in the desired alloy in the form of metal powders and / or one or more metal alloy powders with a binder;
  2. b) production of a green compact by injection molding of the feedstock;
  3. c) preparation of a browning by at least partial removal of the binder from the green compact by catalytic and / or solvent and / or thermal debinding;
  4. d) sintering the at least partially debinded browning to obtain the desired shaped article;
wherein the inventive method is characterized in that in step c) the binder is completely removed, wherein, optionally after performing one or more preceding debinding steps, a thermal debinding takes place to remove the (residual) binder, which is in at least 0.5 Vol .-% oxygen-containing atmosphere is carried out, after which the resulting completely unbonded Braunling is sintered.

Durch dieses Verfahren werden hochreine Formkörper aus Aluminiumlegierungen erhalten, da es aufgrund der vollständigen Entfernung des Binders in Schritt c) zu keinen unerwünschten Reaktionen des Kunststoffs mit den Legierungsmetallen kommt. Diese restlose Entfernung des Binders gelingt - sogar bei relativ niedrigen Temperaturen - aufgrund der Gegenwart von Sauerstoff in der Atmosphäre. Entgegen der herrschenden Lehre, wonach Sauerstoff unbedingt zu vermeiden ist, haben die Erfinder herausgefunden, dass ein geringer Anteil von zumindest 0,5 Vol.-%, die Oxidation des Aluminiums nicht nennenswert fördert, aber zu einer raschen und vollständigen Entbinderung beiträgt. In Abhängigkeit von Zusammensetzung des Pulvergemischs und den Temperaturbedingungen wird beispielsweise ein Sauerstoffanteil zwischen 20 und 100 Vol.-% eingesetzt, d.h. es kann sogar reines O2-Gas eingesetzt werden.By this method, highly pure moldings of aluminum alloys are obtained, since there is no unwanted reactions of the plastic with the alloy metals due to the complete removal of the binder in step c). This complete removal of the binder succeeds - even at relatively low temperatures - due to the presence of oxygen in the atmosphere. Contrary to the prevailing theory that oxygen must be avoided at all costs, the inventors have found that a small proportion of at least 0.5% by volume does not appreciably promote the oxidation of the aluminum, but contributes to rapid and complete debindering. Depending on the composition of the powder mixture and the temperature conditions, for example, an oxygen content between 20 and 100 vol .-% is used, ie it can even be used pure O 2 gas.

Die Aluminiumlegierung enthält neben Aluminium ein oder mehrere andere Metalle, die nicht speziell eingeschränkt sind. Vorzugsweise sind die Legierungspartner aus der aus Magnesium, Kupfer, Silicium und Mangan bestehenden Gruppe ausgewählt und sind besonders bevorzugt in einem jeweiligen Anteil von 0,5 bis 25 Gew.-% enthalten, um Formkörper mit wünschenswerten Eigenschaften zu erhalten. Deutlich niedriger schmelzende Metalle, wie z.B. Bismut, Zinn, Blei, Indium oder auch Zink, oder Legierungen wie etwa Woodsches Metall, die mitunter als Sinterhilfen zur Erniedrigung der Temperatur des Schmelzbeginns dienen, sind gemäß vorliegender Erfindung nicht erforderlich, können jedoch auf Wunsch dennoch als Legierungspartner zugesetzt werden, um Sinterkörper aus den entsprechenden Legierungen zu erhalten. In besonders vorteilhafter Weise werden die weiteren Metalle als Legierungen mit Aluminium, d.h. als Vorlegierungs- oder so genannte Masteralloy-Pulver, eingesetzt.The aluminum alloy contains, besides aluminum, one or more other metals which are not specifically limited. Preferably, the alloying partners are selected from the group consisting of magnesium, copper, silicon and manganese, and are more preferably contained in a respective proportion of 0.5 to 25% by weight to obtain molded articles having desirable properties. Significantly lower melting metals, such as bismuth, tin, lead, indium, or even zinc, or alloys such as Wood's metal, sometimes called sintering aids for lowering serve the temperature of the onset of melting, are not required according to the present invention, but can still be added as alloying partners, if desired, to obtain sintered bodies of the corresponding alloys. In a particularly advantageous manner, the other metals are used as alloys with aluminum, ie as master alloy or so-called master alloy powder.

Gemäß vorliegender Erfindung werden vorzugsweise Binder eingesetzt, die bekanntermaßen bei niedrigen Temperaturen entfernbar sind, besonders bevorzugt Polyacetal-basierte Binder, z.B. Polyoxymethylen- (POM-) Binder, beispielsweise solche, wie sie von BASF in EP 413.231 , WO 94/25205 und vor allem EP 446.708 offenbart und auch unter dem Markennamen Catamold® vertrieben werden. Um die rasche und vollständige Entfernbarkeit bei niedrigen Temperaturen und in Gegenwart von Sauerstoff zu fördern, ist im Binder ein hoher Polyacetal-Anteil wünschenswert, weswegen der Binder vorzugsweise zu 50 bis 95 %, noch bevorzugter zu 80 bis 90 %, aus Polyacetal besteht. Alternativ können auch Bindersysteme zum Einsatz kommen, die auf Wachs-Polymer-Basis aufgebaut sind und bei denen die Hauptkomponente Wachs durch vorhergehende Lösungsentbinderung, d.h. vor der erfindungsgemäßen Durchführung der thermischen Entbinderung in Gegenwart von Sauerstoff, entfernt wird.According to the present invention, it is preferred to use binders which are known to be removable at low temperatures, more preferably polyacetal-based binders, for example polyoxymethylene (POM) binders, for example those described by BASF in US Pat EP 413,231 . WO 94/25205 and especially EP 446,708 disclosed and sold under the brand name Catamold ® . In order to promote rapid and complete removability at low temperatures and in the presence of oxygen, a high polyacetal content is desirable in the binder, and therefore, the binder is preferably 50 to 95%, more preferably 80 to 90%, of polyacetal. Alternatively, binder systems can be used which are based on wax polymer-based and in which the main component wax by previous Lösungsentbinderung, ie prior to the inventive implementation of the thermal debinding in the presence of oxygen, is removed.

Die Entbinderung in Schritt c) des erfindungsgemäßen Verfahrens kann einen einzigen Schritt der thermischen Entbinderung in Gegenwart von Sauerstoff umfassen, in dem der gesamte Binder entfernt wird. Alternativ dazu können ein oder mehrere vorhergehende Entbinderungsschritte durchgeführt werden, um die Hauptmenge des Binders zu entfernen, worauf der erfindungsgemäße thermische Entbinderungsschritt zur Entfernung des Restbinders in Gegenwart von Sauerstoff folgt. So kann ein vorhergehender Entbinderungsschritt ebenfalls eine thermische Entbinderung - in Abwesenheit oder ebenfalls in Gegenwart von Sauerstoff - sein. Das heißt, als Entbinderung kann auch eine mehrstufige thermische Entbinderung bei unterschiedlichen Verfahrensparametern, beispielsweise unterschiedlicher Temperatur oder Atmosphäre, z.B. ohne und mit Sauerstoff oder mit Luft und reinem Sauerstoff usw., durchgeführt werden.Debinding in step c) of the process of the invention may involve a single step of thermal debinding in the presence of oxygen, in which the entire binder is removed. Alternatively, one or more preceding debinding steps may be performed to remove the bulk of the binder, followed by the thermal debinding step of the present invention to remove the residual binder in the presence of oxygen. Thus, a previous debinding step may also be a thermal debindering - in the absence or also in the presence of oxygen. That is, as debindering can also be a multi-stage thermal debindering at different process parameters, such as different temperature or atmosphere, eg without and with oxygen or with air and pure oxygen, etc.

In bevorzugten Ausführungsformen der Erfindung wird in Schritt c) vor der thermischen Entbinderung zur Entfernung des Restbinders in Gegenwart von Sauerstoff zunächst eine katalytische Entbinderung und/oder eine Lösungsentbinderung durchgeführt. Dabei wird bereits die Hauptmenge des Binders aus der Zusammensetzung entfernt, so dass bei der anschließenden thermischen Entbinderung vorzugsweise nur noch die "Backbone"-Komponente entfernt zu werden braucht.In preferred embodiments of the invention, first a catalytic debinding and / or a Lösungsentbinderung performed in step c) before the thermal debinding to remove the residual binder in the presence of oxygen. In this case, the bulk of the binder is already removed from the composition, so that in the subsequent thermal debinding preferably only the "backbone" component needs to be removed.

Die katalytische Entbinderung erfolgt dabei vorzugsweise in Gegenwart zumindest einer Säure, ausgewählt aus Salpetersäure, Oxalsäure, Ameisensäure und Essigsäure, da diese Säuren durch Acidolyse die vollständige Entfernung der bevorzugten Polyacetal-Binder beschleunigen, ohne zu unerwünschten Nebenreaktionen mit den Legierungspartnern zu führen. Im Falle der Lösungsentbinderung wird hingegen die Hauptmenge des Binders durch Extraktion mit einem geeigneten Lösungsmittel oder Lösungsmittelgemisch, wie z.B. Aceton, n-Heptan, Wasser etc., entfernt. Besonders bevorzugt ist gemäß vorliegender Erfindung eine katalytische Entbinderung mit sublimierter Oxalsäure.The catalytic debinding is carried out preferably in the presence of at least one acid selected from nitric acid, oxalic acid, formic acid and acetic acid, since these acids accelerate the complete removal of the preferred polyacetal binder by acidolysis, without leading to undesirable side reactions with the alloying partners. In the case of solution debonding, on the other hand, the bulk of the binder is obtained by extraction with a suitable solvent or solvent mixture, e.g. Acetone, n-heptane, water etc., removed. Particularly preferred according to the present invention is a catalytic debindering with sublimed oxalic acid.

Wie bereits erwähnt wird die thermische Entbinderung zur Entfernung des Restbinders in Schritt c) bei einer relativ niedrigen Temperatur durchgeführt, um Oxidationsreaktionen, vor allem des Aluminiums im Pulvergemisch, zu unterdrücken. Unter einer relativ niedrigen Temperatur ist hierin eine Temperatur deutlich unterhalb des Schmelzpunkts von Aluminium, vorzugsweise unterhalb von 500 °C, noch bevorzugter zwischen 100 und 420 °C, zu verstehen. Insbesondere wird ein für das jeweilige Pulvergemisch empirisch optimiertes Temperaturprofil eingestellt, das vorzugsweise eine Heizrate von nicht mehr als 5 K/min, noch bevorzugter von nicht mehr als 1 bis 2 K/min, vorsieht. Dadurch wird das zu entbindernde Gemisch auf schonende, gleichmäßige Weise erhitzt.As already mentioned, the thermal debinding to remove the residual binder in step c) is carried out at a relatively low temperature in order to suppress oxidation reactions, especially of the aluminum in the powder mixture. By a relatively low temperature herein is meant a temperature well below the melting point of aluminum, preferably below 500 ° C, more preferably between 100 and 420 ° C. In particular, an empirically optimized temperature profile for the respective powder mixture is set, which preferably provides a heating rate of not more than 5 K / min, more preferably not more than 1 to 2 K / min. As a result, the mixture to be debindered is heated in a gentle, uniform manner.

Der Sinterschritt d) des erfindungsgemäßen Verfahrens ist abgesehen von der Anforderung, dass der Binder zuvor vollständig entfernt worden sein muss, nicht speziell eingeschränkt. Vorzugsweise wird jedoch unter Ausbildung einer flüssigen Phase gesintert, wie dies nachstehend näher ausgeführt wird.The sintering step d) of the process of the present invention is not specifically limited except for the requirement that the binder must be completely removed beforehand. Preferably, however, is sintered to form a liquid phase, as will be explained in more detail below.

Die bisher bekannte Technologie der pulvermetallurgischen Formteilherstellung von Aluminiumlegierungen mittels Formpressen beruht auf dem theoretischen Ansatz, dass durch den Pressvorgang in der Matrize die Oberfläche der mit einer Aluminiumoxidschicht überzogenen Aluminiumpartikel mechanisch verletzt wird, wodurch eine metallurgische Reaktion überhaupt erst ermöglicht wird. Bei einem (vollständig) entbinderten Braunkörper aus dem Pulverspritzguss handelt es sich aber de facto um eine Metallpulverschüttung, wobei die Oxidhäute der Metalle keinerlei mechanischer Belastung ausgesetzt waren und deshalb diesem bekannten Mechanismus nicht unterliegen. Das heißt, es gibt hier keine direkten Metall-Metall-Kontakte zwischen den Pulverpartikeln. Trotzdem gelingt es im erfindungsgemäßen Verfahren, durch geeignete Wahl der Sinterbedingungen die erforderliche Schrumpfung zu erzielen, anhand derer sich die Verdichtung des Sinterkörpers manifestiert, und somit weitestgehend dichte Bauteile zu erhalten.The hitherto known technology of powder metallurgical molding of aluminum alloys by means of compression molding is based on the theoretical approach that the surface of the aluminum particles coated with an aluminum oxide layer is mechanically damaged by the pressing process in the matrix, whereby a metallurgical reaction is made possible in the first place. In the case of a (completely) bindered brown body from powder injection molding, however, it is de facto a metal powder spill, with the oxide skins of the metals not being exposed to any mechanical stress and therefore not subject to this known mechanism. That is, there are no direct metal-to-metal contacts between the powder particles. Nevertheless, it is possible in the process according to the invention, by suitable choice of the sintering conditions to achieve the required shrinkage, by means of which manifests the compression of the sintered body, and thus to obtain largely dense components.

Erfindungsgemäß bevorzugt werden daher Ausführungsformen, bei denen der vollständig entbinderte Bräunling in Schritt d) unter Ausbildung einer flüssigen Phase gesintert wird. Diese flüssige Phase, die nach Ansicht der Erfinder - ohne sich auf eine spezielle Theorie festegen zu wollen - zu einem Teil intermediär, aber vorwiegend stationär, d.h. im thermodynamischen Gleichgewicht mit der festen Al-Phase, vorliegt, stellt über Mikrorisse, -poren oder ähnliche "Öffnungen" in den Oxidhäuten der Metallpulverpartikel und Unterwanderung der Oxidhäute den erforderlichen Kontakt zwischen den Metallen im Pulvergemisch her und unterstützt so die Ausbildung eines hochdichten Sinterkörpers aus dem vollständig entbinderten Bräunling. Besonders bevorzugt wird das Sintern in Schritt d) bei einer Temperatur zwischen der Solidus- und der Liquidus-Temperatur der jeweiligen Aluminiumlegierung durchgeführt, so dass zu jedem Zeitpunkt während des Sintervorgangs nur ein durch die Wahl eines entsprechenden Temperaturprofils steuerbarer Anteil der Legierungsmetalle in flüssiger Phase vorliegt, was einen Verlust der Maß- und Formstabilität wirksam verhindert.Embodiments according to the invention are therefore preferred in which the completely debinded browning material is sintered in step d) to form a liquid phase. This liquid phase, which in the view of the inventors - without wishing to be bound to a particular theory - to a part intermediary, but predominantly stationary, ie in thermodynamic equilibrium with the solid Al phase, is present over microcracks, pores or the like "Openings" in the oxide skins of the metal powder particles and infiltration of the oxide skins forth the required contact between the metals in the powder mixture ago and thus supports the formation of a high-density sintered body from the completely unbonded Bräunling. Particularly preferably, the sintering in step d) is carried out at a temperature between the solidus and the liquidus temperature of the respective aluminum alloy, so that at any time during the sintering process only a controllable by the choice of a corresponding temperature profile proportion of the alloy metals in liquid Phase exists, which effectively prevents loss of dimensional and dimensional stability.

Die Zusammensetzung der jeweiligen Atmosphäre in deh einzelnen Schritten des erfindungsgemäßen Verfahrens ist abgesehen von der Gegenwart des Sauerstoffs bei der thermischen Entbinderung in Schritt c) nicht speziell eingeschränkt, und der einschlägige Fachmann kann in jedem einzelnen Schritt die für das jeweilige Pulvergemisch am besten geeignete Atmosphäre wählen, wobei auch Vakuum möglich ist. Der Sinterschritt d) wird jedoch vorzugsweise in extrem trockener stickstoffhältiger Atmosphäre durchgeführt, d.h. in reinem Stickstoff, unter Normaldruck oder reduziertem Druck ("Teildrucksintern"), oder in einem Gemisch aus Stickstoff und reinem Edelgas (Helium, Argon), vorzugsweise mit einem Taupunkt < -40 °C, da die Gegenwart von Stickstoff die Benetzbarkeit der Pulverteilchen mit der entstehenden Metallschmelze maßgeblich unterstützt.The composition of the particular atmosphere in the individual steps of the process according to the invention is not particularly limited except for the presence of the oxygen in the thermal debinding in step c), and the person skilled in the art can select in each individual step the most suitable atmosphere for the respective powder mixture , whereby also vacuum is possible. However, the sintering step d) is preferably carried out in an extremely dry nitrogen-containing atmosphere, i. in pure nitrogen, under normal pressure or reduced pressure ("partial pressure sintering"), or in a mixture of nitrogen and pure inert gas (helium, argon), preferably with a dew point <-40 ° C, since the presence of nitrogen with the wettability of the powder the resulting molten metal significantly supported.

Auf das Sintern kann gegebenenfalls eine geeignete Nachbehandlung folgen, mittels derer die fertigen Formteile in der gewünschten Form erhalten werden. Beispielsweise kann das bekannte Verfahren des heißisostatischen Pressens (HIP) angewandt werden, um die Formteile auf die gewünschte endgültige Dichte zu bringen. Dabei werden nach dem Sintern verbliebene Restporen durch die gleichzeitige Einwirkung von äußerem Gasdruck und Temperatur zugedrückt und die Porenwände miteinander verschweißt.If appropriate, sintering may be followed by a suitable after-treatment, by means of which the finished molded parts are obtained in the desired shape. For example, the known method of hot isostatic pressing (HIP) can be used to bring the moldings to the desired final density. In this case, residual pores remaining after sintering are pressed by the simultaneous action of external gas pressure and temperature, and the pore walls are welded together.

KURZBESCHREIBUNG DER ZEICHNUNGENBRIEF DESCRIPTION OF THE DRAWINGS

  • Fig. 1 ist eine Fotografie des Grünlings (oben) und des daraus erhaltenen Sinterkörpers (unten) aus Beispiel 9. Fig. 1 is a photograph of the green compact (top) and the resulting sintered body (bottom) of Example 9.
  • Fig. 2 ist eine Fotografie des Grünlings (links) und des daraus erhaltenen Sinterkörpers (rechts) aus Beispiel 10. Fig. 2 is a photograph of the green compact (left) and the resulting sintered body (right) of Example 10.

Die Erfindung wird nachstehend anhand von nichteinschränkenden konkreten Ausführungsbeispielen näher beschrieben.The invention will be described below with reference to non-limiting specific embodiments.

BEISPIELEEXAMPLES

Sämtliche in den nachstehenden Beispielen hergestellten Feedstocks wurden in einem beheizten Messkneter bei 190 °C homogenisiert. Aus diesen Feedstocks wurden mittels Spritzguss gemäß ISO 2740 Zugprobestäbe bzw. Hohlzylinder geformt, wobei das erfindungsgemäße Verfahren wie folgt zum Einsatz kam. Zur Herstellung der Grünteile wurde eine hydraulische Spritzgießmaschine (Battenfeld HM 600/130) mit PIM-Ausstattung herangezogen.All feedstocks prepared in the examples below were homogenized in a heated kneader at 190 ° C. From these feedstocks, tensile test bars or hollow cylinders were molded by means of injection molding in accordance with ISO 2740, the method according to the invention being used as follows. To produce the green parts, a hydraulic injection molding machine (Battenfeld HM 600/130) with PIM equipment was used.

In einem ersten Schritt wurde zunächst der Feedstock in einen Trichter der Spritzgießmaschine eingefüllt. Das Pulverspritzgießen zur Herstellung der Grünteile erfolgte in folgenden Schritten: Das aufbereitete Einsatzmaterial wurde mittels eines beheizten Spritzzylinders, in dem sich eine Schnecke dreht, nach voreingestellten Einstellungsparameten (wie z.B. Umdrehungsgeschwindigkeit, Dosiervolumen, Staudruck usw.) plastifiziert und vordosiert. Anschließend wurde in ein entsprechend temperiertes Werkzeug die vordosierte Menge eingespritzt. In Abhängigkeit vom Feedstock bzw. eingesetzten Binder betrug die Plastifizierungstemperatur im Spritzzylinder zwischen 120 und 220 °C, während im Werkzeug zwischen 25 bis 140 °C herrschten. Nach ausreichender Kühlzeit wurde das Spritzgießwerkzeug geöffnet und der Grünteil aus dem Werkzeug ausgeworfen und mit einem Handling entnommen.In a first step, the feedstock was first filled into a funnel of the injection molding machine. The powder injection molding for the production of the green parts was carried out in the following steps: The prepared feed material was plasticized and pre-dosed by means of a heated injection cylinder in which a screw rotates according to preset setting parameters (such as, for example, rotational speed, metering volume, dynamic pressure, etc.). Subsequently, the pre-dosed quantity was injected into a suitably tempered tool. Depending on the feedstock or binder used, the plasticizing temperature in the injection cylinder was between 120 and 220 ° C, while in the tool between 25 and 140 ° C prevailed. After sufficient cooling time, the injection mold was opened and the green part ejected from the tool and removed with a handling.

Beispiel 1 - Zugstäbe: Lösungsentbinderung/thermische EntbinderungExample 1 - Tension rods: Solution debonding / thermal debinding

Ein im Handel erhältliches Metallpulvergemisch (Alumix® 231 von Ecka), bestehend aus Aluminium mit 14 Gew.-% Silicium, 2,5 Gew.-% Kupfer und 0,6 Gew.-% Magnesium, wurde mit einem aus Wachs/Thermoplast bestehenden Solventbinder sorgfältig zu einem Feedstock vermischt. Feedstock-Komponente Anteil (Gew.-%) Alumix 231-Pulver* 74,8 Solventbinder: Wachsanteil 14,8 Solventbinder: Thermoplastanteil 8,2 Stearinsäure 2,2 100,0 * Im Handel erhältliches Metallpulvergemisch aus Aluminium mit 14 Gew.-% Silicium, 2,5 Gew.-% Kupfer und 0,6 Gew.-% Magnesium (von Ecka) A commercially available metal powder mixture (Alumix ® 231 of Ecka) consisting of aluminum, with 14 wt .-% of silicon, 2.5 wt .-% copper and 0.6 wt .-% magnesium, was with a group consisting of wax / thermoplastic Solvent binder carefully mixed into a feedstock. Feedstock component Proportion (% by weight) Alumix 231 powder * 74.8 Solvent binder: wax content 14.8 Solvent binder: thermoplastic content 8.2 stearic acid 2.2 100.0 * Commercially available metal powder mixture of aluminum with 14% by weight of silicon, 2.5% by weight of copper and 0.6% by weight of magnesium (from Ecka)

Entbinderung und Sintern der ZugstäbeDebinding and sintering of the tension rods

Dieser Feedstock wurde zunächst mittels Solventextraktion in einem 60-I-Ofen mit Aceton bei einer Temperatur von 45 °C innerhalb von 12 h entbindert.This feedstock was first debinded by solvent extraction in a 60 L oven with acetone at a temperature of 45 ° C over 12 h.

Der so erhaltene Bräunling enthielt einen Restbinderanteil von rund 14,5 Gew.-%, der anschließend durch erfindungsgemäße thermische Entbinderung mittels eines Temperaturprofils von 150 °C bis 320 °C für 1 h und danach von 320 bis 420 °C für 1,5 h mit einer Heizrate von 3 K/min unter einer reinen Sauerstoff enthaltenden Atmosphäre entfernt wurde. Der somit vollständig entbinderte Bräunling wurde danach bei 560 °C innerhalb 1 h in reinem Stickstoff (Taupunkt: -50 °C) gesintert.The Bräunling thus obtained contained a residual binder content of about 14.5 wt .-%, which then by thermal debinding according to the invention by means of a temperature profile of 150 ° C to 320 ° C for 1 h and then from 320 to 420 ° C for 1.5 h was removed at a heating rate of 3 K / min under a pure oxygen-containing atmosphere. The thus completely unbonded Bräunling was then sintered at 560 ° C within 1 h in pure nitrogen (dew point: -50 ° C).

ErgebnisseResults

  • Längenschwindung: 11,6 %Length shrinkage: 11.6%
  • Schwindung des Stabdurchmessers: 12,25 %Shrinkage of the bar diameter: 12.25%
  • Sinterdichte: 2,36 g/cm3 Sintered density: 2.36 g / cm 3
Beispiel 2 - Zugstäbe: thermische Entbinderung in einem SchrittExample 2 - Tension rods: thermal debindering in one step

Feedstock-KomponenteFeedstock component Anteil (Gew.-%)Proportion (% by weight) Aluminiumpulveraluminum powder 67,167.1 Masteralloy-Pulver*Master Alloy Powder * 4,34.3 POM-BinderPOM Binder 25,825.8 Lucryl G55**Lucryl G55 ** 2,82.8 100,0100.0 * Vorlegierung aus Aluminium und Magnesium im Verhältnis 50:50
** Im Handel erhältliches Polymethylmethacrylat (PMMA; von BASF)
* Master alloy of aluminum and magnesium in the ratio 50:50
** Commercially available polymethylmethacrylate (PMMA, from BASF)

Entbinderung und Sintern der ZugstäbeDebinding and sintering of the tension rods

Hier wurde eine vollständige thermische Entbinderung in einem 40-I-Ofen mit 200 l/h reinem Sauerstoff nach folgendem Entbinderungsprofil durchgeführt:

  • Aufheizen auf 130 °C mit einer Heizrate von 2 K/min
  • 4 h Haltezeit bei 130 °C
  • Aufheizen auf 200 °C mit einer Heizrate von 2 K/min
  • 5 h Haltezeit bei 200 °C
  • Aufheizen auf 420 °C mit einer Heizrate von 2 K/min
  • 4 h Haltezeit bei 420 °C
Der Gewichtsverlust nach der thermischen Entbinderung betrug 24,2 %.Here a complete thermal debindering was carried out in a 40 l oven with 200 l / h of pure oxygen according to the following debindering profile:
  • Heating to 130 ° C with a heating rate of 2 K / min
  • 4 h hold time at 130 ° C
  • Heating to 200 ° C with a heating rate of 2 K / min
  • 5 h hold time at 200 ° C
  • Heating to 420 ° C with a heating rate of 2 K / min
  • 4 h hold time at 420 ° C
Weight loss after thermal debinding was 24.2%.

Anschließend erfolgte das Sintern bei einer Ofeneinstelltemperatur von 665 °C, die einer Temperatur innerhalb des Ofens von etwa 630 °C entspricht, während 1 h in reinem Stickstoff.Subsequently, the sintering was carried out at a furnace setting temperature of 665 ° C, which corresponds to a temperature within the furnace of about 630 ° C, during 1 h in pure nitrogen.

ErgebnisseResults

  • Längenschwindung: 12,27 %Length shrinkage: 12.27%
  • Schwindung des Stabdurchmessers: 14,52 %Shrinkage of the bar diameter: 14.52%
  • Sinterdichte: 2,46 g/cm3 Sintered density: 2.46 g / cm 3
Beispiel 3 - Zugstäbe: zweifache thermische EntbinderungExample 3 - Tension rods: double thermal debinding

Feedstock-KomponenteFeedstock component Anteil (Gew.-%)Proportion (% by weight) Aluminiumpulveraluminum powder 70,170.1 Magnesiumpulvermagnesium powder 2,22.2 POM-BinderPOM Binder 24,024.0 Tensid*surfactant * 3,73.7 100,0100.0 * Ethoxylierter C13-C15-Oxoalkohol mit 7 EO-Einheiten* Ethoxylated C 13 -C 15 oxo alcohol with 7 EO units

Entbinderung und Sintern der ZugstäbeDebinding and sintering of the tension rods

Zunächst erfolgte eine erste thermische Entbinderung in einem 50-I-Ofen in 500 l/h Luft bei 180 °C während 14 h. Gewichtsverlust: 27,0 %.First, a first thermal debinding was carried out in a 50 l oven in 500 l / h of air at 180 ° C for 14 h. Weight loss: 27.0%.

Anschließend erfolgte eine zweite thermische Entbinderung bis 420 °C unter reinem Sauerstoff innerhalb 1 h, wonach wiederum bei einer Ofeneinstelltemperatur von 665 °C 1 h lang unter Stickstoff gesintert wurde.This was followed by a second thermal debindering to 420 ° C under pure oxygen within 1 h, which in turn was sintered under nitrogen at a Ofeneinstelltemperatur of 665 ° C for 1 h.

ErgebnisseResults

  • Längenschwindung: 9,5 %Length shrinkage: 9.5%
  • Schwindung des Stabdurchmessers: 11,4 %Shrinkage of the bar diameter: 11.4%
  • Sinterdichte: 2,13 g/cm3 Sintered density: 2.13 g / cm 3
Beispiel 4 - Zugstäbe: katalytische/thermische EntbinderungExample 4 - Tensile Bars: Catalytic / Thermal Debinding

Feedstock-KomponenteFeedstock component Anteil (Gew.-%)Proportion (% by weight) Aluminiumpulveraluminum powder 70,170.1 Magnesiumpulvermagnesium powder 2,22.2 POM-BinderPOM Binder 24,024.0 Tensid*surfactant * 3,73.7 100,0100.0 * Ethoxylierter C13-C15-Oxoalkohol mit 7 EO-Einheiten* Ethoxylated C 13 -C 15 oxo alcohol with 7 EO units

Entbinderung und Sintern der ZugstäbeDebinding and sintering of the tension rods

Zunächst erfolgte eine katalytische Entbinderung in einem 50-I-Ofen mit 2 Vol-% HNO3 in 500 l/h Stickstoff (technisch rein) bei 140 °C während 10 h. Gewichtsverlust: 22,1 %. Dabei zeigten sich perlenähnliche Auswüchse auf der Oberfläche, die sich vermutlich durch Reaktion des Mg mit HNO3 gebildet hatten.First, a catalytic debinding in a 50-liter oven with 2% by volume of HNO 3 in 500 l / h of nitrogen (technically pure) at 140 ° C for 10 h. Weight loss: 22.1%. There were pearl-like outgrowths on the surface, which were probably formed by reaction of Mg with HNO 3 .

Anschließend erfolgte wie in Beispiel 3 eine thermische Entbinderung bis 420 °C unter reinem Sauerstoff innerhalb 1 h, wonach erneut bei einer Ofeneinstelltemperatur von 665 °C 1 h lang unter Stickstoff gesintert wurde.Subsequently, as in Example 3, a thermal debindering to 420 ° C under pure oxygen within 1 h, after which it was again sintered at a Ofeneinstelltemperatur of 665 ° C for 1 h under nitrogen.

ErgebnisseResults

  • Längenschwindung: 10,7 %Length shrinkage: 10.7%
  • Schwindung des Stabdurchmessers: 14,65 %Shrinkage of the bar diameter: 14.65%
  • Sinterdichte: 2,36 g/cm3 Sintered density: 2.36 g / cm 3
Beispiel 5 - Zugstäbe: katalytische/thermische Entbinderung Example 5 - Tensile Bars: Catalytic / Thermal Debinding

Feedstock-KomponenteFeedstock component Anteil (Gew.-%)Proportion (% by weight) Aluminiumpulveraluminum powder 70,170.1 Magnesiumpulvermagnesium powder 2,22.2 POM-BinderPOM Binder 24,024.0 Tensid*surfactant * 3,73.7 100,0100.0 * Ethoxylierter C13-C15-Oxoalkohol mit 7 EO-Einheiten* Ethoxylated C 13 -C 15 oxo alcohol with 7 EO units

Entbinderung und Sintern der ZugstäbeDebinding and sintering of the tension rods

Zunächst erfolgte eine katalytische Entbinderung analog zu Beispiel 4, jedoch unter Einsatz von 80 g wasserfreier Oxalsäure auf einer Sublimierschale anstelle der HNO3 bei 140 °C während 24 h. Gewichtsverlust: 23,0 %. Aufgrund der Verwendung von Oxalsäure zeigten sich keine Auswüchse auf der Oberfläche. Anschließend erfolgten thermische Entbinderung und Sintern ebenfalls analog zu Beispiel 4.First, a catalytic debinding was carried out analogously to Example 4, but using 80 g of anhydrous oxalic acid on a Sublimierschale instead of HNO 3 at 140 ° C for 24 h. Weight loss: 23.0%. Due to the use of oxalic acid, no outgrowths appeared on the surface. Subsequently, thermal debinding and sintering were also carried out analogously to Example 4.

ErgebnisseResults

  • Längenschwindung: 14,28 %Length shrinkage: 14.28%
  • Schwindung des Stabdurchmessers: 15,68 %Shrinkage of the bar diameter: 15.68%
  • Sinterdichte: 2,42 g/cm3 Sintered density: 2.42 g / cm 3
Beispiel 6 - Zugstäbe: katalytische/thermische EntbinderungExample 6 - Tensile Bars: Catalytic / Thermal Debinding

Feedstock-KomponenteFeedstock component Anteil (Gew.-%)Proportion (% by weight) Alumix 231-Pulver*Alumix 231 powder * 70,870.8 POM-Binder*POM Binder * 25,625.6 Tensid**surfactant ** 3,63.6 100,0100.0 * Im Handel erhältliches Metallpulvergemisch aus Aluminium mit 14 Gew.-% Silicium, 2,5 Gew.-% Kupfer und 0,6 Gew.-% Magnesium (von Ecka)
** Ethoxylierter C13-C15-Oxoalkohol mit 7 EO-Einheiten
* Commercially available metal powder mixture of aluminum with 14% by weight of silicon, 2.5% by weight of copper and 0.6% by weight of magnesium (from Ecka)
** Ethoxylated C 13 -C 15 oxo alcohol with 7 EO units

Entbinderung und Sintern der ZugstäbeDebinding and sintering of the tension rods

Zunächst erfolgte eine katalytische Entbinderung analog zu Beispiel 5. Gewichtsverlust: 25,2 %. Anschließend erfolgten thermische Entbinderung und Sintern analog zu Beispiel 4, allerdings bei einer Ofeneinstelltemperatur von 560 °C.First, a catalytic debinding was carried out analogously to Example 5. Weight loss: 25.2%. Subsequently, thermal debinding and sintering were carried out analogously to Example 4, but at a Ofeneinstelltemperatur of 560 ° C.

ErgebnisseResults

  • Längenschwindung: 11,2 %Length shrinkage: 11.2%
  • Schwindung des Stabdurchmessers: 13,2 %Shrinkage of the bar diameter: 13.2%
  • Sinterdichte: 2,45 g/cm3 Sintered density: 2.45 g / cm 3
Beispiel 7 - Zugstäbe: katalytische/thermische Entbinderung Example 7 - Tensile Bars: Catalytic / Thermal Debinding

Feedstock-KomponenteFeedstock component Anteil (Gew.-%)Proportion (% by weight) Aluminiumpulveraluminum powder 68,068.0 Masteralloy-Pulver*Master Alloy Powder * 4,34.3 POM-BinderPOM Binder 24,024.0 Tensid**surfactant ** 3,73.7 100,0100.0 * Vorlegierung aus Aluminium und Magnesium im Verhältnis 50:50
** Ethoxylierter C13-C15-Oxoalkohol mit 7 EO-Einheiten
* Master alloy of aluminum and magnesium in the ratio 50:50
** Ethoxylated C 13 -C 15 oxo alcohol with 7 EO units

Entbinderung und Sintern der ZugstäbeDebinding and sintering of the tension rods

Zunächst erfolgte eine katalytische Entbinderung analog zu Beispiel 5. Gewichtsverlust: 23,2 %. Anschließend erfolgten thermische Entbinderung und Sintern analog zu Beispiel 4.First, a catalytic Entbinderung analogous to Example 5. Weight loss: 23.2%. Subsequently, thermal debinding and sintering were carried out analogously to Example 4.

ErgebnisseResults

  • Längenschwindung: 12,6 %Length shrinkage: 12.6%
  • Schwindung des Stabdurchmessers: 13,25 %Shrinkage of the rod diameter: 13.25%
  • Sinterdichte: 2,56 g/cm3 Sintered density: 2.56 g / cm 3
Beispiel 8 - Hohlzylinder: katalytische/thermische Entbinderung Example 8 - Hollow Cylinder: Catalytic / Thermal Debinding

Feedstock-KomponenteFeedstock component Anteil (Gew.-%)Proportion (% by weight) Aluminiumpulveraluminum powder 68,068.0 Masteralloy-Pulver*Master Alloy Powder * 4,34.3 POM-BinderPOM Binder 24,024.0 Tensid**surfactant ** 3,73.7 100,0100.0 * Vorlegierung aus Aluminium und Magnesium im Verhältnis 50:50
** Ethoxylierter C13-C15-Oxoalkohol mit 7 EO-Einheiten
* Master alloy of aluminum and magnesium in the ratio 50:50
** Ethoxylated C 13 -C 15 oxo alcohol with 7 EO units

Entbinderung und Sintern der HohlzylinderDebinding and sintering of the hollow cylinder

Zunächst erfolgte eine katalytische Entbinderung analog zu Beispiel 5. Gewichtsverlust: 23,7 %. Anschließend erfolgten thermische Entbinderung und Sintern analog zu Beispiel 4.First, a catalytic debinding was carried out analogously to Example 5. Weight loss: 23.7%. Subsequently, thermal debinding and sintering were carried out analogously to Example 4.

ErgebnisseResults

  • Höhenschwindung: 17,24 %Height shrinkage: 17.24%
  • Schwindung des Durchmessers: 14,48 %Shrinkage of the diameter: 14.48%
  • Sinterdichte: 2,59 g/cm3 Sintered density: 2.59 g / cm 3
Beispiel 9 - Zugstäbe: katalytische/thermische Entbinderung Example 9 - Tensile Bars: Catalytic / Thermal Debinding

Feedstock-KomponenteFeedstock component Anteil (Gew.-%)Proportion (% by weight) Aluminiumpulveraluminum powder 67,167.1 Masteralloy-Pulver*Master Alloy Powder * 4,34.3 POM-Binder*POM Binder * 25,825.8 Lucryl G55**Lucryl G55 ** 2,82.8 100,0100.0 * Vorlegierung aus Aluminium und Magnesium im Verhältnis 50:50
** Im Handel erhältliches Polymethylmethacrylat (PMMA; von BASF)
* Master alloy of aluminum and magnesium in the ratio 50:50
** Commercially available polymethylmethacrylate (PMMA, from BASF)

Entbinderung und Sintern der ZugstäbeDebinding and sintering of the tension rods

Zunächst erfolgte eine katalytische Entbinderung analog zu Beispiel 5. Gewichtsverlust: 25,7 %. Anschließend erfolgten thermische Entbinderung und Sintern analog zu Beispiel 4.First, a catalytic debinding analogous to Example 5. Weight loss: 25.7%. Subsequently, thermal debinding and sintering were carried out analogously to Example 4.

ErgebnisseResults

  • Längenschwindung: 13,57 %Length shrinkage: 13.57%
  • Schwindung des Stabdurchmessers: 19,55 %Shrinkage of the bar diameter: 19.55%
  • Sinterdichte: 2,59 g/cm3 Sintered density: 2.59 g / cm 3
Beispiel 10 - Hohlzylinder: katalytische/thermische EntbinderungExample 10 - Hollow Cylinder: Catalytic / Thermal Debinding

Feedstock-KomponenteFeedstock component Anteil (Gew.-%)Proportion (% by weight) Aluminiumpulveraluminum powder 67,167.1 Masteralloy-Pulver*Master Alloy Powder * 4,34.3 POM-BinderPOM Binder 25,825.8 Lucryl G55**Lucryl G55 ** 2,82.8 100,0100.0 * Vorlegierung aus Aluminium und Magnesium im Verhältnis 50:50
** Im Handel erhältliches Polymethylmethacrylat (PMMA; von BASF)
* Master alloy of aluminum and magnesium in the ratio 50:50
** Commercially available polymethylmethacrylate (PMMA, from BASF)

Entbinderung und Sintern der HohlzylinderDebinding and sintering of the hollow cylinder

Zunächst erfolgte eine katalytische Entbinderung analog zu Beispiel 5. Gewichtsverlust: 25,6 %. Anschließend erfolgten thermische Entbinderung und Sintern analog zu Beispiel 4.First, a catalytic debinding analogous to Example 5. Weight loss: 25.6%. Subsequently, thermal debinding and sintering were carried out analogously to Example 4.

ErgebnisseResults

  • Höhenschwindung: 16,52 %Height shrinkage: 16.52%
  • Schwindung des Durchmessers: 14,48 %Shrinkage of the diameter: 14.48%
  • Sinterdichte: 2,56 g/cm3 Sintered density: 2.56 g / cm 3

Somit können durch das erfindungsgemäße Verfahren Sinterkörper aus Aluminiumlegierungen mittels Spritzguss bereitgestellt werden, die für den praktischen Einsatz auf vielerlei Gebieten, z.B. auf dem Verkehrssektor, im Bauwesen, im Maschinenbau, in der Verpackungsindustrie, Eisen- und Stahlindustrie, Elektrotechnik, in Haushaltsgeräten usw., beispielsweise zur Wärmeableitung in elektronischen Geräten ("heat sinks") oder als Komponenten von Klimaanlagen, bestens geeignet sind.Thus, by the method according to the invention sintered bodies of aluminum alloys can be provided by means of injection molding, which are suitable for practical use in many fields, e.g. in the transport sector, construction, mechanical engineering, packaging, iron and steel, electrical engineering, household appliances, etc., for example for heat dissipation in electronic devices ("heat sinks") or as components of air conditioning systems.

Claims (19)

  1. A method for producing molded articles based on aluminum alloys by metal powder injection molding, comprising the following steps:
    a) producing a feedstock by mixing the metals contained in the desired alloy in the form of metal powders and/or one or more metal alloy powders with a binder;
    b) producing a green body by injection molding said feedstock;
    c) producing a brown body by removing the binder from the green body by catalytic and/or solvent and/or thermal debinding;
    d) sintering the at least partially debound brown body to obtain the desired molded article;
    characterized in that, in step (c), said binder is completely removed, wherein, optionally after having carried out one or more previous debinding steps, thermal debinding is carried out to remove the binder or residual binder, said thermal debinding being carried in an atmosphere containing at least 0.5 % by volume of oxygen, whereafter the thus obtained completely debound brown body is sintered.
  2. The method according to claim 1, characterized in that, in addition to aluminum, the aluminum alloy contains one or more metals selected from magnesium, copper, silicon, and manganese.
  3. The method according to claim 1 or 2, characterized in that, in addition to aluminum, the aluminum alloy contains one or more metals at a perecentage of 0.5 to 25 % by weight, respectively.
  4. The method according to any one of claims 1 to 3, characterized in that the metal(s) is/are used as (a) master alloy powder(s).
  5. The method according to any one of the preceding claims, characterized in that a polyacetal-based binder, e.g., polyoxymethylene (POM) binder, is used as said binder.
  6. The method according to claim 5, characterized in that said binder consists of 50 to 95 % of polyacetal.
  7. The method according to claim 6, characterized in that said binder consists of 80 to 90 % of poylacetal.
  8. The method according to any one of claims 1 to 7, characterized in that, in step (c), only thermal debinding in the presence of oxygen is conducted in one or more steps in which the binder is completely removed.
  9. The method according to any one of claims 1 to 7, characterized in that, in step (c), solvent debinding to remove the main part of the binder, followed by said thermal debinding to remove the residual binder are conducted.
  10. The method according to any one of claims 1 to 7, characterized in that, in step (c), catalytic debinding to remove the main part of the binder, followed by said thermal debinding to remove the residual binder are conducted.
  11. The method according to claim 10, characterized in that said catalytic debinding is carried out in the presence of at least one acid selected from nitric acid, oxalic acid, formic acid, and acetic acid.
  12. The method according to claim 11, characterized in that sublimated oxalic acid is used as the acid.
  13. The method according to any one of the preceding claims, characterized in that said thermal debinding to remove the residual binder is carried out at a temperature below 500 °C.
  14. The method according to claim 13, characterized in that said thermal debinding to remove the residual binder is carried out applying a specific temperature profile ranging between 100 and 420 °C.
  15. The method according to claim 13 or 14, characterized in that the heating rate during said thermal debinding process for removing the residual binder does not exceed 5 K/min.
  16. The method according to claim 15, characterized in that the heating rate does not exceed 1 to 2 K/min.
  17. The method according to any one of the preceding claims, characterized in that, in step d), the completely debound brown body is sintered while forming a liquid phase.
  18. The method according to claim 17, characterized in that sintering is carried out at a temperature between the solidus and the liquidus temperatures of the respective aluminum alloy.
  19. The method according to any one of the preceding claims, characterized in that the heating rate to reach the sintering temperature after said thermal debinding step for removing the residual binder ranges from 4 to 20 K/min.
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WO2010149648A1 (en) 2009-06-25 2010-12-29 Basf Se Method for the continuous thermal debinding of a thermoplastic molding compound
CN104057089A (en) * 2013-03-20 2014-09-24 江苏天一超细金属粉末有限公司 Metal, ceramic powder and polymer mixture used for manufacturing metal and ceramic products and method for removing polymer from moldings by acid catalysis
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GB2513869B (en) * 2013-05-07 2015-12-30 Charles Grant Purnell Aluminium alloy products, and methods of making such alloy products
CN104227002A (en) * 2013-06-19 2014-12-24 东莞市事通达机电科技有限公司 Metallurgical injection molding process of aluminum powder
CN103769587A (en) * 2013-11-28 2014-05-07 王利民 Method and device for producing metal 3D printing method product
TWI669330B (en) * 2018-05-23 2019-08-21 晟銘電子科技股份有限公司 Shot material composition for metal injection molding,molded article and preparing method thereof
CN108889950A (en) * 2018-06-21 2018-11-27 深圳市富优驰科技有限公司 A kind of preparation method of hollow radiator and hollow radiator
US11219960B2 (en) 2019-05-29 2022-01-11 The Boeing Company Flash-removal tool
US10724932B1 (en) * 2019-05-29 2020-07-28 The Boeing Company Monolithic precursor test coupons for testing material properties of metal-injection-molded components
US11229951B2 (en) 2019-05-29 2022-01-25 The Boeing Company Monolithic precursor test coupons for testing material properties of metal-injection-molded components and methods and apparatuses for making such coupons
CN113878116A (en) * 2021-10-11 2022-01-04 深圳艾利佳材料科技有限公司 Sintering method of thin-wall strip part based on profiling jig
WO2023156610A1 (en) 2022-02-18 2023-08-24 Basf Se A process for the treatment of at least one three-dimensional green body

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0329475B1 (en) * 1988-02-18 1994-01-26 Sanyo Chemical Industries Ltd. Mouldable composition
JP3128130B2 (en) * 1989-08-16 2001-01-29 ビーエーエスエフ アクチェンゲゼルシャフト Method for producing inorganic sintered compact
US5176740A (en) * 1989-12-29 1993-01-05 Showa Denko K.K. Aluminum-alloy powder, sintered aluminum-alloy, and method for producing the sintered aluminum-alloy
DE4007345A1 (en) 1990-03-08 1991-09-12 Basf Ag THERMOPLASTIC MEASURES FOR THE PRODUCTION OF METALLIC MOLDED BODIES
JPH06192706A (en) * 1992-12-25 1994-07-12 Sanyo Chem Ind Ltd Method for degreasing sinterable powder compact
DE4314694C1 (en) 1993-05-04 1994-05-11 Basf Ag Prepn. of sinter mouldings from a mixt. of a sinterable powder and an oxymethylene binding agent - involving removal of binding agent by treatment with a gaseous acid which is solid at room temp.
CA2133387A1 (en) * 1993-10-01 1995-04-02 Basf K&F Corporation Process for improving the debinding rate of ceramic and metal injection molded products
JPH0820803A (en) * 1993-11-22 1996-01-23 Sanyo Chem Ind Ltd Production of sintered compact
EP0701875B1 (en) * 1994-09-15 2000-06-07 Basf Aktiengesellschaft Process for preparing metallic articles by injection moulding
JP2000017304A (en) * 1998-06-29 2000-01-18 Olympus Optical Co Ltd Production of inorganic powder sintered compact and inorganic powder sintered compact
JP2000063903A (en) * 1998-08-13 2000-02-29 Citizen Watch Co Ltd Manufacture of power injection-molded parts
US6376585B1 (en) * 2000-06-26 2002-04-23 Apex Advanced Technologies, Llc Binder system and method for particulate material with debind rate control additive
US7691174B2 (en) * 2004-03-08 2010-04-06 Battelle Memorial Institute Feedstock composition and method of using same for powder metallurgy forming a reactive metals
CA2660484A1 (en) * 2006-08-07 2008-02-14 The University Of Queensland Metal injection moulding method
KR20080027171A (en) * 2006-09-22 2008-03-26 세이코 엡슨 가부시키가이샤 Method for producing sintered body and sintered body
WO2010149648A1 (en) * 2009-06-25 2010-12-29 Basf Se Method for the continuous thermal debinding of a thermoplastic molding compound

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

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AT509613A1 (en) 2011-10-15
ES2639134T3 (en) 2017-10-25
WO2011120066A1 (en) 2011-10-06
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US20130101456A1 (en) 2013-04-25
EP2552630A1 (en) 2013-02-06
DK2552630T3 (en) 2017-09-25
KR20130079373A (en) 2013-07-10
PL2552630T3 (en) 2018-05-30
SG184423A1 (en) 2012-10-30
JP5956419B2 (en) 2016-07-27
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JP2013524006A (en) 2013-06-17
AT509613B1 (en) 2017-05-15

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