EP3004220A1 - Method for the thermal treatment of poly-arylene ether ketone ketone powders suitable for laser sintering - Google Patents

Method for the thermal treatment of poly-arylene ether ketone ketone powders suitable for laser sintering

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Publication number
EP3004220A1
EP3004220A1 EP14731735.8A EP14731735A EP3004220A1 EP 3004220 A1 EP3004220 A1 EP 3004220A1 EP 14731735 A EP14731735 A EP 14731735A EP 3004220 A1 EP3004220 A1 EP 3004220A1
Authority
EP
European Patent Office
Prior art keywords
powder
minutes
pekk
less
ketone
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.)
Withdrawn
Application number
EP14731735.8A
Other languages
German (de)
French (fr)
Inventor
Nadine Decraemer
Denis Huze
Hervé Ster
Jerome Pascal
Benoît BRULE
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Arkema France SA
Original Assignee
Arkema France SA
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Arkema France SA filed Critical Arkema France SA
Publication of EP3004220A1 publication Critical patent/EP3004220A1/en
Withdrawn legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L61/00Compositions of condensation polymers of aldehydes or ketones; Compositions of derivatives of such polymers
    • C08L61/04Condensation polymers of aldehydes or ketones with phenols only
    • C08L61/16Condensation polymers of aldehydes or ketones with phenols only of ketones with phenols
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B13/00Conditioning or physical treatment of the material to be shaped
    • B29B13/02Conditioning or physical treatment of the material to be shaped by heating
    • B29B13/021Heat treatment of powders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C67/00Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00
    • B29C67/02Moulding by agglomerating
    • B29C67/04Sintering
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/34Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives
    • C08G65/38Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols
    • C08G65/40Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives derived from phenols from phenols (I) and other compounds (II), e.g. OH-Ar-OH + X-Ar-X, where X is halogen atom, i.e. leaving group
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/12Powdering or granulating
    • C08J3/124Treatment for improving the free-flowing characteristics
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2071/00Use of polyethers, e.g. PEEK, i.e. polyether-etherketone or PEK, i.e. polyetherketone or derivatives thereof, as moulding material
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2650/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G2650/28Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule characterised by the polymer type
    • C08G2650/38Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule characterised by the polymer type containing oxygen in addition to the ether group
    • C08G2650/40Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule characterised by the polymer type containing oxygen in addition to the ether group containing ketone groups, e.g. polyarylethylketones, PEEK or PEK
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2371/00Characterised by the use of polyethers obtained by reactions forming an ether link in the main chain; Derivatives of such polymers
    • C08J2371/08Polyethers derived from hydroxy compounds or from their metallic derivatives
    • C08J2371/10Polyethers derived from hydroxy compounds or from their metallic derivatives from phenols

Definitions

  • the present invention relates to a rapid process for heat treatment of polyarylene-ether-ketone-ketone powder suitable for laser sintering, as well as the powders resulting from this process.
  • the present invention relates to a method for the thermal treatment of polyarylene-ether-ketone-ketone powders adapted to laser sintering. process.
  • Polyarylene ether ketones and more particularly polyether ketone ketones (PEKK) are very effective materials. They are used for demanding applications in temperature and / or in mechanical stresses, even chemical. These polymers are found in fields as varied as aeronautics, offshore drilling, medical implants. They can be implemented by molding, extrusion, compression, spinning or laser sintering in particular. However, their implementation in the latter process requires powder preparation conditions ensuring good flowability in times prohibitive on the industrial level.
  • Powder sintering technology under a laser beam is used to manufacture three-dimensional objects such as prototypes, models, but also functional parts, especially in the automotive, nautical, aeronautical, aerospace, medical (prosthetic, auditory systems) fields. , cellular tissues ...), textiles, clothing, fashion, decoration, housings for electronics, telephony, home automation, computers, lighting.
  • a thin layer of powder is deposited on a horizontal plate held in a chamber heated to a certain temperature.
  • the laser brings the necessary energy to sinter the powder particles at different points of the powder layer according to a geometry corresponding to the object, for example using a computer having in memory the shape of the object and restoring the latter in the form of slices.
  • the horizontal plate is lowered by a value corresponding to the thickness of a layer of powder (for example between 0.05 and 2 mm and generally of the order of 0.1 mm) and then a new layer is deposited. of powder and the laser provides the energy necessary to sinter the powder particles in a geometry corresponding to this new slice of the object and so on.
  • the procedure is repeated until the whole object has been made.
  • An object surrounded by unsintered powder is obtained inside the enclosure. Parts that were not sintered therefore remained in powder form.
  • the object is separated from the powder which can be reused for another operation.
  • One of the conditions necessary to obtain a good operation of the laser sintering method consists of using powders having a good flowability necessary during the layering of the powder described above.
  • US7847057 relates to a method of thermal treatment of poly-arylene-ether-ketone powders consisting of exposing the powder to a heat treatment greater than 30 minutes and of preferably greater than 1 hour, at a temperature of 20 ° C higher than the glass transition temperature of the polymer.
  • WO2012047613 also describes a heat treatment applied more particularly to PEKK powders consisting of exposing the powder to a heat treatment lasting several hours between the transition temperatures of the different crystalline phases, more particularly by approaching the melting temperature of the polymer, corresponding to the crystalline form having the transition at the highest temperature.
  • the flowability of the powder is improved and the resulting crystallinity of this treatment is retained during the sintering process, giving the sintered object some advantageous physical properties.
  • the processing times are relatively long, typically several hours, which is industrially disadvantageous (machine occupation and low productivity).
  • the invention relates to a process for the treatment of powders comprising PEKK, the measured flowability of which has a funneling time of 17 mm of less than 40 s, including the limit, preferably less than 30 s, and even more preferably less than 20 s. s, the flowability being measured as follows:
  • the invention also relates to the powders obtained by such a process, as well as to the objects obtained by the process using such powders. Detailed description :
  • polyarylene-ether-ketone ketones used in the invention comprise units of formulas IA, of formula IB and their mixture:
  • polyarylene-ether-ketone-ketones corresponding to the generic names PEK, PEEKEK, PEEK, PEKEKK (or E denotes an ether function and K a ketone function) can not be ruled out, particularly when their use is combined with that of PEKK in proportions where the PEKK represents more than 50% in mass proportions and preferably more than 80% in proportions by mass, limits understood.
  • the polyarylene ether ketone ketones are polyesters having a mixture of the units IA and IB such that the mass percentage of terephthalic unit by relation to the sum both the isophthalic and isophthalic units range from 55% to 85% and preferably from 55% to 70%, most preferably 60%.
  • terephthalic and isophthalic unit is meant the formula of the acidic and isophthalic acids, respectively.
  • These polyarylene-ether-ketone ketones are in the form of powders that may have been prepared by grinding or precipitation.
  • the powders or powder mixtures used in the process which is the subject of the invention can be obtained for example by a grinding method described in application FR 1160258. They may optionally be additive or contain different compounds such as reinforcing fillers, especially mineral fillers such as carbon black, nanotubes, carbon or not, fibers, milled or not, stabilizing agents (light, in particular UV, and heat), agents facilitating the flow such as silica or optical brighteners, dyes, pigments or a combination of these fillers and / or additives.
  • reinforcing fillers especially mineral fillers such as carbon black, nanotubes, carbon or not, fibers, milled or not
  • stabilizing agents light, in particular UV, and heat
  • agents facilitating the flow such as silica or optical brighteners, dyes, pigments or a combination of these fillers and / or additives.
  • the treatment time will typically be strictly less than 30 minutes, ideally between 15 and 25 minutes while in a dynamic heating system such as a tube in which the powder and a hot gas circulates against the current, or a heated fluidized bed, a residence time of the order of a few minutes, may be sufficient, typically greater than 2 minutes but less than 30 minutes and preferably between 2 and 15 minutes.
  • the treatment can also be performed in a pallet dryer, a dryer with a vertical axis, in a rotary kiln, or under a tunnel heated with infrared lamps.
  • the powder resulting from this heat treatment is then used in a powder sintering device under a laser beam to allow the manufacture of an object.
  • the use of such powders in processes such as rotational molding can not be ruled out. Examples:
  • the powder is placed in a crystallizer so that the thickness of the powder bed is between 1 and 1.5 cm.
  • the powders were sieved on a vibrating screen of 250 ⁇ m to de-agglomerate.
  • the Dv50 referred to here is the volume median diameter which corresponds to the value of the particle size that divides the particle population examined in exactly two.
  • the Dv50 is measured according to the ISO 9276 standard - parts 1 to 6. In the present description, a Malvern Mastersizer 2000 particle size analyzer is used, and the measurement is made in liquid way by laser diffraction on the powder. The results are given in Table 1 for residence times ranging from 15 minutes to 25 minutes.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

The invention relates to a method for the thermal treatment of poly-arylene ether ketone ketone powder suitable for laser sintering, and to the powders obtained by this method.

Description

Procédé de traitement thermique de poudres de Polyarylène- éther-cétone-cétone adaptées au frittage laser La présente invention concerne un procédé rapide de traitement thermique de poudre de Polyarylène-éther-cétone- cétones adaptées au frittage laser, ainsi que les poudres issues de ce procédé. Les poly-arylène-éther-cétones et plus particulièrement les Poly éther-cétone-cétones (PEKK) sont des matériaux très performants. Ils sont utilisés pour des applications contraignantes en température ou/et en contraintes mécaniques, voire chimiques. On retrouve ces polymères dans des domaines aussi variés que l'aéronautique, les forages off shore, les implants médicaux. Ils peuvent être mis en oeuvre par moulage, extrusion, compression, filage, ou encore frittage laser notamment. Cependant, leur mise en œuvre dans ce dernier procédé nécessite des conditions de préparation de la poudre assurant une bonne coulabilité dans des temps prohibitifs sur le plan industriel.  The present invention relates to a rapid process for heat treatment of polyarylene-ether-ketone-ketone powder suitable for laser sintering, as well as the powders resulting from this process. BACKGROUND OF THE INVENTION The present invention relates to a method for the thermal treatment of polyarylene-ether-ketone-ketone powders adapted to laser sintering. process. Polyarylene ether ketones and more particularly polyether ketone ketones (PEKK) are very effective materials. They are used for demanding applications in temperature and / or in mechanical stresses, even chemical. These polymers are found in fields as varied as aeronautics, offshore drilling, medical implants. They can be implemented by molding, extrusion, compression, spinning or laser sintering in particular. However, their implementation in the latter process requires powder preparation conditions ensuring good flowability in times prohibitive on the industrial level.
La technologie de frittage de poudres sous un faisceau laser sert à fabriquer des objets en trois dimensions tels que des prototypes, des modèles, mais aussi des pièces fonctionnelles, notamment dans les domaines automobile, nautique, aéronautique, aérospatial, médical (prothèses, systèmes auditifs, tissus cellulaires...) , le textile, l'habillement, la mode, la décoration, des boîtiers pour l'électronique, la téléphonie, la domotique, l'informatique, 1 ' éclairage . Powder sintering technology under a laser beam is used to manufacture three-dimensional objects such as prototypes, models, but also functional parts, especially in the automotive, nautical, aeronautical, aerospace, medical (prosthetic, auditory systems) fields. , cellular tissues ...), textiles, clothing, fashion, decoration, housings for electronics, telephony, home automation, computers, lighting.
On dépose une fine couche de poudre sur une plaque horizontale maintenue dans une enceinte chauffée à une certaine température. Le laser apporte l'énergie nécessaire à fritter les particules de poudre en différents points de la couche de poudre selon une géométrie correspondant à l'objet, par exemple à l'aide d'un ordinateur ayant en mémoire la forme de l'objet et restituant cette dernière sous forme de tranches. Ensuite, on abaisse la plaque horizontale d'une valeur correspondant à l'épaisseur d'une couche de poudre (par exemple entre 0,05 et 2 mm et généralement de l'ordre de 0,1 mm) puis on dépose une nouvelle couche de poudre et le laser apporte l'énergie nécessaire à fritter les particules de poudre selon une géométrie correspondant à cette nouvelle tranche de l'objet et ainsi de suite. La procédure est répétée jusqu'à ce que l'on ait fabriqué tout l'objet. On obtient à l'intérieur de l'enceinte un objet entouré de poudre non frittée. Les parties qui n'ont pas été frittées sont donc restées à l'état de poudre. Après complet refroidissement, on sépare l'objet de la poudre qui peut être réutilisée pour une autre opération. A thin layer of powder is deposited on a horizontal plate held in a chamber heated to a certain temperature. The laser brings the necessary energy to sinter the powder particles at different points of the powder layer according to a geometry corresponding to the object, for example using a computer having in memory the shape of the object and restoring the latter in the form of slices. Then, the horizontal plate is lowered by a value corresponding to the thickness of a layer of powder (for example between 0.05 and 2 mm and generally of the order of 0.1 mm) and then a new layer is deposited. of powder and the laser provides the energy necessary to sinter the powder particles in a geometry corresponding to this new slice of the object and so on. The procedure is repeated until the whole object has been made. An object surrounded by unsintered powder is obtained inside the enclosure. Parts that were not sintered therefore remained in powder form. After complete cooling, the object is separated from the powder which can be reused for another operation.
Une des conditions nécessaire à l'obtention d'un bon fonctionnement du procédé de frittage laser consiste à utiliser des poudres présentant une bonne coulabilité nécessaire lors de la mise en couche de la poudre décrite ci-dessus. One of the conditions necessary to obtain a good operation of the laser sintering method consists of using powders having a good flowability necessary during the layering of the powder described above.
Malheureusement, les poudres issues des procédés de broyage, précipitation ou atomisation à la fusion ne permettent pas d'obtenir des poudres de bonne coulabilité. Un traitement thermique long doit être appliqué afin d'obtenir une poudre présentant une bonne coulabilité. Unfortunately, the powders resulting from grinding, precipitation or fusion atomization processes do not make it possible to obtain good flowability powders. A long heat treatment must be applied in order to obtain a powder having a good flowability.
Jusqu'à présent il n'a pas été possible d'obtenir une bonne coulabilité dans un temps industriellement acceptable, typiquement largement inférieur à une heure.  Until now it has not been possible to obtain good flowability in an industrially acceptable time, typically well below one hour.
US7847057 concerne un procédé de traitement thermique de poudres de poly-arylène-éther-cétones consistant à exposer la poudre à un traitement thermique supérieur à 30 minutes et de préférence supérieur à 1 heure, à une température supérieure de 20 °C à la température de transition vitreuse du polymère. US7847057 relates to a method of thermal treatment of poly-arylene-ether-ketone powders consisting of exposing the powder to a heat treatment greater than 30 minutes and of preferably greater than 1 hour, at a temperature of 20 ° C higher than the glass transition temperature of the polymer.
Ce traitement appliqué sur des Poly-éther-éther-cétones permet d'obtenir des poudres de coulabilité acceptable pour le procédé de frittage laser mais est très long ce qui limite l'intérêt industriel. Ce traitement thermique permet de rendre la surface de la poudre de PEEK moins rugueuse ce qui explique leur meilleure coulabilité. Une réduction du temps de traitement augmenterait l'attrait industriel en augmentant la productivité de traitement de la poudre. This treatment applied to polyether-ether-ketones makes it possible to obtain acceptable flowable powders for the laser sintering process but is very long, which limits the industrial interest. This heat treatment makes the surface of the PEEK powder less rough, which explains their better flowability. A reduction in processing time would increase the industrial appeal by increasing the productivity of powder processing.
WO2012047613 décrit également un traitement thermique appliqué plus particulièrement aux poudres de PEKK consistant à exposer la poudre à un traitement thermique de plusieurs heures entre les températures de transition des différentes phases cristallines, plus particulièrement en se rapprochant de la température de fusion du polymère, correspondant à la forme cristalline présentant la transition à la plus haute température. La coulabilité de la poudre s'en trouve améliorée et la cristallinité résultante de ce traitement est conservée durant le procédé de frittage, conférant à l'objet fritté certaines propriétés physiques avantageuses. Ici encore, les temps de traitement sont relativement longs, typiquement plusieurs heures, ce qui est industriellement pénalisant (occupation machine et faible productivité) . WO2012047613 also describes a heat treatment applied more particularly to PEKK powders consisting of exposing the powder to a heat treatment lasting several hours between the transition temperatures of the different crystalline phases, more particularly by approaching the melting temperature of the polymer, corresponding to the crystalline form having the transition at the highest temperature. The flowability of the powder is improved and the resulting crystallinity of this treatment is retained during the sintering process, giving the sintered object some advantageous physical properties. Here again, the processing times are relatively long, typically several hours, which is industrially disadvantageous (machine occupation and low productivity).
Pour répondre aux besoins de disposer de poudres présentant une bonne coulabilité, la demanderesse a conduit une série de tests mettant en évidence contre toute attente que pour certains PEKK, un traitement thermique approprié bien plus court assure l'obtention de poudres présentant le critère de bonne coulabilité. Résumé de l'invention: In order to meet the needs of having powders having good flowability, the applicant has conducted a series of tests showing against all odds that for some PEKK, a suitable heat treatment much shorter ensures the obtaining of powders presenting the criterion of good flowability. Summary of the invention
L' invention concerne un procédé de traitement de poudres comprenant du PEKK dont la coulabilité mesurée présente un temps de passage en entonnoir de 17 mm inférieure à 40 s, borne comprise, de préférence inférieure à 30 s, et de façon encore préférée inférieure à 20 s, la dite coulabilité étant mesurée de la façon suivante :  The invention relates to a process for the treatment of powders comprising PEKK, the measured flowability of which has a funneling time of 17 mm of less than 40 s, including the limit, preferably less than 30 s, and even more preferably less than 20 s. s, the flowability being measured as follows:
Remplir un entonnoir en verre d'orifice 17 mm avec la poudre jusqu'à 5 mm du bord. Boucher l'orifice du bas avec le doigt,  Fill a 17 mm glass funnel with the powder up to 5 mm from the edge. Close the bottom hole with your finger,
Mesurer au chronomètre le temps d'écoulement de la poudre Measure at the stopwatch the flow time of the powder
Si l'écoulement ne se fait pas, taper sur l'entonnoir à l'aide d'une spatule. Répéter l'opération si besoin,If flow does not occur, tap the funnel with a spatula. Repeat the operation if necessary
Noter le temps d'écoulement et le nombre de coups tapés à l'aide de la spatule, comprenant les étapes suivantes : Note the flow time and number of strokes typed using the spatula, including the following steps:
-Disposition de la poudre dans une enceinte ventilée ou tout autre système de chauffage.  -Disposition of the powder in a ventilated enclosure or any other heating system.
-Chauffage de la poudre à une température comprise entre T-10°C et T +10°C, ou T = 3.75 * A+ 37.5 , exprimée en °C, A représentant le pourcentage massique en motif t é répht a 1 i que par rapport à la somme des motifs térépht al ique et isophtalique et est compris entre 55 % et 85 %, bornes comprises, durant un temps strictement inférieur à 30 minutes.  -Heating the powder at a temperature between T-10 ° C and T + 10 ° C, or T = 3.75 * A + 37.5, expressed in ° C, A representing the mass percentage in repeating pattern at 1 i by to the sum of the terephthalic and isophthalic units and is between 55% and 85%, inclusive, for a time strictly less than 30 minutes.
L' invention concerne également les poudres obtenues par un tel procédé, ainsi que les objets obtenus par le procédé utilisant de telles poudres. Description détaillée : The invention also relates to the powders obtained by such a process, as well as to the objects obtained by the process using such powders. Detailed description :
Les Polyarylène-éther-cétone-cétones utilisés dans l'invention comprennent des motifs de formules IA, de formule IB et leur mélange :  The polyarylene-ether-ketone ketones used in the invention comprise units of formulas IA, of formula IB and their mixture:
Formule IA Formula IA
On ne saurait exclure dans un cadre plus général, les Polyarylène-éther-cétone-cétones répondant aux noms génériques PEK, PEEKEK, PEEK, PEKEKK (ou E désigne une fonction éther et K une fonction cétone) en particulier lorsque leur utilisation se fait de façon combinée à celle du PEKK dans des proportions ou le PEKK représente plus de 50 % en proportions massique et de préférence plus de 80 % en proportions massique, bornes compr i ses. In a more general context, polyarylene-ether-ketone-ketones corresponding to the generic names PEK, PEEKEK, PEEK, PEKEKK (or E denotes an ether function and K a ketone function) can not be ruled out, particularly when their use is combined with that of PEKK in proportions where the PEKK represents more than 50% in mass proportions and preferably more than 80% in proportions by mass, limits understood.
De préférence les Polyarylène-éther-cétone-cétones sont des Po 1 y- é the r - cé t o ne s - cé t o ne s comprenant un mélange des motifs IA et IB de telle sorte que le pourcentage massique en motif térépht al ique par rapport à la somme des motifs t é r épht a 1 i que et isophtalique soit compris entre 55% et 85% et de préférence entre 55% et 70%, idéalement 60%. Par motif térépht al ique et isophtalique, on entend la formule des acides t é r épht a 1 i que et isophtalique respectivement. Preferably, the polyarylene ether ketone ketones are polyesters having a mixture of the units IA and IB such that the mass percentage of terephthalic unit by relation to the sum both the isophthalic and isophthalic units range from 55% to 85% and preferably from 55% to 70%, most preferably 60%. By terephthalic and isophthalic unit is meant the formula of the acidic and isophthalic acids, respectively.
Ces Poly-arylène-éther-cétone-cétones se présentent sous forme de poudres pouvant avoir été préparées par broyage ou précipitation. These polyarylene-ether-ketone ketones are in the form of powders that may have been prepared by grinding or precipitation.
Ils se présentent après le procédé de traitement thermique de l'invention sous forme d'une poudre dont la coulabilité en entonnoir de 17 mm est inférieure à 40 s borne comprise et de préférence inférieure à 30 s, et de façon encore préférée inférieure à 20 s. They are presented after the heat treatment process of the invention in the form of a powder whose funnel flowability of 17 mm is less than 40 s inclusive and preferably less than 30 s, and more preferably less than 20 s. s.
Les poudres ou mélanges de poudres utilisés dans le procédé objet de l'invention peuvent être obtenues par exemple par un procédé de broyage décrit dans la demande FR 1160258. Elles peuvent le cas échéant être additivées ou contenir différents composés tel des charges renforçantes, notamment des charges minérales telles que le noir de carbone, des nanotubes, de carbone ou non, des fibres, broyées ou non, des agents stabilisants (lumière, en particulier UV, et chaleur) , des agents facilitant l'écoulement tel que la silice ou encore des azurants optiques, colorants, pigments ou une combinaison de ces charges et/ou additifs. The powders or powder mixtures used in the process which is the subject of the invention can be obtained for example by a grinding method described in application FR 1160258. They may optionally be additive or contain different compounds such as reinforcing fillers, especially mineral fillers such as carbon black, nanotubes, carbon or not, fibers, milled or not, stabilizing agents (light, in particular UV, and heat), agents facilitating the flow such as silica or optical brighteners, dyes, pigments or a combination of these fillers and / or additives.
Le procédé de traitement de telles poudres conformes à l'invention et permettant d'obtenir les poudres conformes à l'invention consiste à faire séjourner la poudre dans un dispositif maintenu en température, typiquement entre une température T-10°C et T +10°C, ou T = 3.75 * A+ 37.5 , exprimée en °C (A représentant le pourcentage massique en motif térépht al ique par rapport à la somme des motifs térépht al ique et isophtalique et compris entre 55% et 85% et de préférence entre 55% et 70%, idéalement 60%), de préférence entre T-5°C et T+5°C, et de façon encore préférentielle entre T-3°C et T+3°C, idéalement T durant des temps strictement inférieurs à 30 minutes. En effet il a été constaté que la température optimum dépend de la proportion massique en motif téréphtalique par rapport à la somme des motifs téréphtalique et isophtalique selon la relation linéaire T = 3.75 * A+ 37.5. On ne sortirait pas du cadre de l'invention en réalisant plusieurs traitements thermiques successifs (à la même température ou à deux températures différentes comprises entre T-10°C et T +10°C, ouThe process for treating such powders in accordance with the invention and making it possible to obtain the powders in accordance with the invention consists in keeping the powder in a device maintained at a temperature, typically between a temperature T-10 ° C and T +10 ° C, or T = 3.75 * A + 37.5, expressed in ° C (A is the terephthalic unit weight percentage relative to the sum of terephthalic and isophthalic units and between 55% and 85% and preferably between 55% and 70%, ideally 60%), preferably between T-5 ° C and T + 5 ° C, and more preferably between T-3 ° C and T + 3 ° C, ideally T for times strictly less than 30 minutes. Indeed, it has been found that the optimum temperature depends on the mass proportion of terephthalic unit with respect to the sum of the terephthalic and isophthalic units according to the linear relationship T = 3.75 * A + 37.5. It would not depart from the scope of the invention by carrying out several successive heat treatments (at the same temperature or at two different temperatures between T-10 ° C and T + 10 ° C, or
T = 3.75 * A+ 37.5 , exprimée en °C, A représentant le pourcentage massique en motif téréphtalique par rapport à la somme des motifs téréphtalique et isophtalique. En étuve statique par exemple, le temps de traitement sera typiquement inférieur strictement à 30 minutes, idéalement entre 15 et 25 minutes tandis que dans un système de chauffage dynamique tel qu'un tube dans lequel circule à contre courant la poudre et un gaz chaud, ou encore un lit fluidisé chauffé, un temps de séjour de l'ordre de quelques minutes, peut être suffisant, typiquement supérieur à 2 minutes mais inférieur strictement à 30 minutes et de façon préférée entre 2 et 15 minutes. Le traitement pourra aussi être effectué dans un sécheur à palette, un sécheur avec axe vertical, dans un four rotatif, ou encore sous un tunnel chauffé à l'aide de lampes infrarouge. T = 3.75 * A + 37.5, expressed in ° C, where A is the weight percent terephthalic unit based on the sum of the terephthalic and isophthalic units. In a static oven for example, the treatment time will typically be strictly less than 30 minutes, ideally between 15 and 25 minutes while in a dynamic heating system such as a tube in which the powder and a hot gas circulates against the current, or a heated fluidized bed, a residence time of the order of a few minutes, may be sufficient, typically greater than 2 minutes but less than 30 minutes and preferably between 2 and 15 minutes. The treatment can also be performed in a pallet dryer, a dryer with a vertical axis, in a rotary kiln, or under a tunnel heated with infrared lamps.
La poudre issue de ce traitement thermique est ensuite utilisée dans un dispositif de frittage de poudres sous un faisceau laser afin de permettre la fabrication d'un objet. On ne saurait exclure l'utilisation de telles poudres dans des procédé tels que le rotomoulage. Exemples : The powder resulting from this heat treatment is then used in a powder sintering device under a laser beam to allow the manufacture of an object. The use of such powders in processes such as rotational molding can not be ruled out. Examples:
Exemple 1 : mesure de la coulabilité : Example 1: measurement of flowability:
La coulabilité de ces poudres a été réalisée dans un entonnoir en verre :  The flowability of these powders was carried out in a glass funnel:
Remplir un entonnoir en verre d'orifice 17 mm (figure 1) avec la poudre jusqu'à 5mm du bord Boucher l'orifice du bas avec le doigt  Fill a 17 mm hole glass funnel (Figure 1) with the powder up to 5 mm from the edge. Cap the bottom hole with your finger.
Mesurer au chronomètre le temps d'écoulement de la poudre - Si l'écoulement ne se fait pas, taper sur l'entonnoir à l'aide d'une spatule. Répéter l'opération si besoin  Measure the flow time of the powder at the stopwatch - If the flow does not occur, tap the funnel with a spatula. Repeat the operation if necessary
Noter le temps d'écoulement et le nombre de coups tapés à l'aide de la spatule. Exemple 2 :  Note the flow time and the number of hits typed using the spatula. Example 2
Une poudre Kepstan® 6003 de la société Arkema, contenant 60 % de motifs téréphtaliques par rapport à la somme des motifs térépht al ique et i s opht a 1 i que , dont la taille de particule présente un dv50 de 50ym plus ou moins 5ym est soumise à un traitement thermique de 260 °C en étuve ventilée dans un cristallisoir . On dispose la poudre dans un cristallisoir de telle sorte que l'épaisseur du lit de poudre soit compris entre 1 et 1.5 cm.  A Kepstan® 6003 powder from Arkema, containing 60% terephthalic units relative to the sum of the terephthalic units and is ophthalmic, whose particle size has a dv50 of 50m +/- 5m is subject to a heat treatment of 260 ° C in a ventilated oven in a crystallizer. The powder is placed in a crystallizer so that the thickness of the powder bed is between 1 and 1.5 cm.
Après traitement, les poudres ont été tamisées sur un tamis vibrant de 250 ym pour les dés-agglomérer .  After treatment, the powders were sieved on a vibrating screen of 250 μm to de-agglomerate.
Le Dv50 appelé ici est le diamètre médian en volume qui correspond à la valeur de la taille de particule qui divise la population de particules examinée exactement en deux. Le Dv50 est mesuré selon la norme ISO 9276 - parties 1 à 6. Dans la présente description, on utilise un granulomètre Malvern Mastersizer 2000, et la mesure est faite en voie liquide par diffraction laser sur la poudre. Les résultats sont donnés au tableau 1 pour des temps de séjours variant de 15 minutes à 25 minutes. The Dv50 referred to here is the volume median diameter which corresponds to the value of the particle size that divides the particle population examined in exactly two. The Dv50 is measured according to the ISO 9276 standard - parts 1 to 6. In the present description, a Malvern Mastersizer 2000 particle size analyzer is used, and the measurement is made in liquid way by laser diffraction on the powder. The results are given in Table 1 for residence times ranging from 15 minutes to 25 minutes.
Tableau 1 : On constate que la coulabilité est améliorée dès 15 min de traitement thermique (écoulement en 35 s versus 48 s) . Un traitement thermique de 25 min améliore de manière très significative la coulabilité de la poudre. Le terme multi est employé lorsque l'on tape sur l'entonnoir continuellement . Table 1: It is found that the flowability is improved after 15 min of heat treatment (flow in 35 s versus 48 s). A heat treatment of 25 min significantly improves the flowability of the powder. The term multi is used when you tap on the funnel continuously.

Claims

Revendications claims
1 Procédé de traitement de poudres comprenant du PEKK dont la coulabilité mesurée présente un temps de passage en entonnoir de 17 mm inférieure à 40 s, borne comprise, de préférence inférieure à 30 s, et de façon encore préférée inférieure à 20 s, la dite coulabilité étant mesurée de la façon suivante : A process for the treatment of powders comprising PEKK, the measured flowability of which has a funneling time of 17 mm of less than 40 seconds, including the limit, preferably less than 30 seconds, and even more preferably less than 20 seconds, the said flowability being measured as follows:
- Remplir un entonnoir en verre d'orifice 17 mm avec la  - Fill a 17 mm glass funnel with the
poudre jusqu'à 5 mm du bord. Boucher l'orifice du bas avec le doigt,  powder up to 5 mm from the edge. Close the bottom hole with your finger,
Mesurer au chronomètre le temps d'écoulement de la poudre Measure at the stopwatch the flow time of the powder
Si l'écoulement ne se fait pas, taper sur l'entonnoir à l'aide d'une spatule. Répéter l'opération si besoin, If flow does not occur, tap the funnel with a spatula. Repeat the operation if necessary
Noter le temps d'écoulement et le nombre de coups tapés à l'aide de la spatule, comprenant les étapes suivantes :  Note the flow time and number of strokes typed using the spatula, including the following steps:
-Disposition de la poudre dans une enceinte ventilée ou tout autre système de chauffage  -Disposition of the powder in a ventilated enclosure or any other heating system
-Chauffage de la poudre à une température comprise entre T-10°C et T +10°C, ou T = 3.75 * A+ 37.5 , exprimée en °C, A représentant le pourcentage massique en motif t é répht a 1 i que par rapport à la somme des motifs t é répht a 1 i que et isophtalique compris entre 55 % et 85 % et durant un temps strictement inférieur à 30 minutes.  -Heating the powder at a temperature between T-10 ° C and T + 10 ° C, or T = 3.75 * A + 37.5, expressed in ° C, A representing the mass percentage in repeating pattern at 1 i by in relation to the sum of the isophthalic and isophthalic units of between 55% and 85% and for a time strictly less than 30 minutes.
2 Procédé selon la revendication 1 dans lequelle en plus du PEKK on adjoint une poudre de PEK, PEEKEK, PEEK,Process according to Claim 1, in which, in addition to PEKK, a powder of PEK, PEEKEK or PEEK is added.
PEKEKK, dans des proportions massiques telles que le PEKK représente plus de 50 %. 3 Procédé selon la re endication 1 dans lequel le PEKK contient une charge. PEKEKK, in mass proportions such that PEKK represents more than 50%. Process according to claim 1 in which the PEKK contains a filler.
4 Procédé selon la revendication 1 dans lequel le PEKK contient au moins un additif. The process of claim 1 wherein the PEKK contains at least one additive.
5 Procédé selon la revendication 1 dans lequel l'enceinte ventilée est une étuve statique. 6 Procédé selon la revendication 1 dans lequel l'enceinte ventilée est un lit fluidisé. The method of claim 1 wherein the ventilated enclosure is a static oven. The method of claim 1 wherein the ventilated enclosure is a fluidized bed.
7 Procédé selon la revendication 1 dans lequel l'enceinte ventilée est un tube dans lequel circule à contre courant de l'air chaud et la poudre. 7. The method of claim 1 wherein the ventilated chamber is a tube in which circulates against hot air and powder.
8 Procédé selon la revendication 5 dans lequel le temps de séjour est supérieur à 15 minutes mais inférieur strictement à 30 minutes. The method of claim 5 wherein the residence time is greater than 15 minutes but less than 30 minutes.
9 Procédé selon les revendications 6 ou 7 dans lequel le temps de séjour est supérieur à 2 minutes mai s i nférieur strictement à 30 minute s . The process of claims 6 or 7 wherein the residence time is greater than 2 minutes but less than 30 minutes.
EP14731735.8A 2013-05-30 2014-05-27 Method for the thermal treatment of poly-arylene ether ketone ketone powders suitable for laser sintering Withdrawn EP3004220A1 (en)

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US10882215B2 (en) 2015-12-28 2021-01-05 Arkema Inc. Processes for producing polymer powders
US10370530B2 (en) * 2016-02-26 2019-08-06 Ricoh Company, Ltd. Methods for solid freeform fabrication
FR3048430B1 (en) * 2016-03-04 2019-08-30 Arkema France POLY- (ARYL-ETHER-KETONE) POWDER (PAEK) SUITABLE FOR SEVERAL TIMES IN SINTERING PROCESSES
CN106752805B (en) * 2017-01-25 2019-09-10 山东凯盛新材料股份有限公司 The preparation method of coating polyether ketone ketone fine powder
US11426928B2 (en) * 2017-09-18 2022-08-30 Solvay Specialty Polymers Usa, Llc Additive manufacturing method for making a three-dimensional object using selective laser sintering
EP3744751B1 (en) * 2018-01-22 2022-08-17 DIC Corporation Polyarylene ether ketone resin and production method therefor, and molded article
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KR20010050170A (en) * 1999-08-31 2001-06-15 조셉 에스. 바이크 Process for Bulk Handling Granular Polybutadiene
DE102004062761A1 (en) * 2004-12-21 2006-06-22 Degussa Ag Use of polyarylene ether ketone powder in a three-dimensional powder-based tool-less production process, and moldings produced therefrom
WO2012047613A1 (en) * 2010-09-27 2012-04-12 Arkema Inc. Heat treated polymer powders
FR2982519B1 (en) * 2011-11-10 2020-02-21 Arkema France PROCESS OF CRUSHING POLYARYL ETHER CETONES
FR3006316B1 (en) * 2013-05-30 2015-05-29 Arkema France COMPOSITION OF POLYARYLENE-ETHER-KETONE-KETONE POWDERS SUITABLE FOR LASER SINTERING

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
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