PROCESS FOR DENSIFICATION OF POLY(ARYLENE ETHER KETONE) POWDERS

Abstract

Process for densification of a poly(arylene ether ketone) (PAEK) powder or of a mixture of poly(arylene ether ketone) (PAEK) powders, the process being mixing the powder or the mixture of powders, in a mixer equipped with a rotary stirrer including at least one blade, for a period of between 30 minutes and 120 minutes, preferably of between 30 and 60 minutes, at a blade-tip speed of between 30 m/s and 70 m/s, preferably of between 40 and 50 m/s.

Claims

1. Process for densification of a poly(arylene ether ketone) (PAEK) powder or of a mixture of poly(arylene ether ketone) (PAEK) powders, wherein the process consists of mixing the powder or the mixture of powders, in a mixer equipped with a rotary stirrer comprising at least one blade, for a period of between 30 minutes and 120 minutes, at a blade-tip speed of between 30 m/s and 70 m/s.

2. Densification process according to claim 1, wherein, during the mixing, the temperature of the powder increases up to a temperature below the lowest glass transition temperature among the PAEKs.

3. Densification process according to claim 1, wherein the mixer is thermally regulated such that the temperature is below 40° C. for all or part of the mixing.

4. Densification process according to claim 1, wherein the powder used is a powder of poly(ether ketone ketone) (PEKK) having a weight percentage of terephthalic units, relative to the sum of the terephthalic and isophthalic units, of between 55% and 85%.

5. Densification process according to claim 4, wherein the powder used comprises, in addition to the PEKK, a powder chosen from at least one of the following powders: PEK, PEEKEK, PEEK and PEKEKK, the PEKK powder representing more than 50% by weight, limit included.

6. Densification process according to claim 1, characterized in that wherein the PAEK powder also comprises at least one filler.

7. Densification process according to claim 1, wherein the PAEK powder also comprises at least one additive.

8. A method of producing an object from a powder densified in accordance with the process according to claim 1, the process comprising producing the object by means of a technology chosen from one of the following technologies: laser sintering, powder coating, compression moulding or transfer moulding.

9. Object produced by means of a technology chosen from one of the following technologies: laser sintering, powder coating, compression moulding or transfer moulding, from a powder densified in accordance with the process according to claim 1.

Description

[0021] Other advantages and characteristics of the invention will emerge on reading the following description given by way of illustrative and non-limiting example, with reference to the appended

[0022] FIG. 1 which represents three curves indicating the change in density of three samples of powder as a function of the time of thermomechanical treatment applied to these three samples.

DESCRIPTION OF THE INVENTION

[0023] Density is defined as the ratio of the weights by volume between the material considered and that of water, and does not therefore have a unit. However, in the interests of uniformity with what is often read in the literature, density can be likened to the weight per volume and can be expressed in kg/m.sup.3.

[0024] The tapped density corresponds to the ratio of the weight of a sample of powder to the volume of this sample, said sample of powder having been tapped before the volume was measured. In the case of the non-tapped density, the sample of powder is not tapped before its volume is measured.

[0025] The PAEKs used in the process which is the subject of the invention comprise especially PEKKs, in particular an isomer thereof or a mixture of the isomers thereof. However, in a more general context, it would not be possible to exclude all of the poly(arylene ether ketone)s, in particular those corresponding to the generic names PEK, PEEK, PEEKEK and PEKEKK, where E denotes an ether function and K denotes a ketone function, in particular when they are used in combination with PEKK in weight proportions where the PEKK represents more than 50% by weight proportion and preferably more than 80% by weight proportion, limits included.

[0026] Preferably, the poly(arylene ether ketone)s are poly(ether ketone ketone)s comprising a mixture of terephthalic and isophthalic units such that the weight percentage of terephthalic units, relative to the sum of the terephthalic and isophthalic units, is between 55% and 85% and preferably between 55% and 70%, ideally 60%. The term “terephthalic and isophthalic unit” is intended to mean the formula of terephthalic acid and of isophthalic acid respectively.

[0027] The PAEK powders, or mixtures of powders, used in the process which is the subject of the invention can be obtained by milling or by precipitation, for example. They can, for example, be obtained in accordance with the milling process described in particular in application FR 1 160 258. They can, where appropriate, comprise one or more additives or contain various compounds, such as fillers, in particular inorganic fillers such as carbon black, carbon or non-carbon nanotubes, milled or unmilled fibres, stabilizing agents (light-stabilizing, in particular UV-stabilizing, and heat-stabilizing), flow-facilitating agents, such as silica, or else optical brighteners, dyes or pigments, or a combination of these fillers and/or additives.

[0028] After having undergone the thermomechanical treatment process of the invention, the PAEK powder exhibits a gain in tapped density of greater than 20% and preferably greater than 40% compared with the powder before treatment.

[0029] The process for treating such powders, which makes it possible to obtain the powders of which the tapped density is significantly increased, consists in mixing the PAEK powder or the mixture of powders, in particular of PEKK, in a rapid commercial mixer, such as the rapid mixers sold by the companies Henschel, Diosna, Eirich, Lodige or Kahl, for example. Such a rapid mixer is equipped with a rotary shaft comprising at least one blade. The powder is mixed for a period of between 30 and 120 minutes, preferably of between 30 and 60 minutes, limits included, at a blade-tip speed of the mixer of between 30 m/s and 70 m/s, preferably of between 40 and 50 m/s. The mixing of the powder can be carried out with or without thermal regulation of the mixer. Such a thermal regulation can be carried out during all or part of the mixing step. It generally amounts to cooling the mixer such that the temperature during the mixing remains below 40° C. Such a thermal regulation of the mixer makes it possible to obtain an improved density, with a gain in tapped density of between 20% and 30% compared with the initial powder.

[0030] Without thermal regulation, the temperature of the powder increases during the mixing step owing to the friction between the powder and the mixer. The mechanical treatment applied to the powder therefore makes it possible to raise its temperature to a temperature of generally between 80 and 100° C. Such a temperature is below the glass transition temperature of the PEKK used, and below the lowest glass transition temperature among the poly(arylene ether ketone)s used, in the case of a mixture of polymers. Indeed, the glass transition temperature of poly(arylene ether ketone)s is generally between 130° C. and 190° C. This heating temperature is also well below the thermal treatment described in document U.S. Pat. No. 7,847,057, the temperature of which is at least 20° C. above the glass transition temperature. The synergy between the mechanical treatment and the thermal heating of the powder makes it possible to obtain a significantly increased densification of the powder, with a greater than 50% gain in tapped density compared with the initial powder.

[0031] The powder obtained has a significantly higher density than the starting powder. The gain in density obtained is different depending on whether or not the mixer is temperature-regulated, and is generally between 20% and 60%. Typically, the gain in density obtained with cooling of the mixer is greater than or equal to 20%, whereas, without cooling of the mixer, it is greater than or equal to 50%.

[0032] The process according to the invention therefore makes it possible to obtain, in particular, PAEK powders which have a density significantly higher than the initial powders. An advantage of this densification process is that it comprises only one step, and allows rapid treatment of the powders. The process is also simple to carry out and is applicable to all PAEK powders having undergone or not undergone prior thermal or mechanical treatments. The thermomechanical stresses applied thus make it possible to obtain powders with a very high density compared with the initial powders. A large gain in density has in particular the following advantages: for the same amount of powder, the amount of air to be eliminated is smaller so that the obtaining of objects with no porosity is thereby facilitated. Owing to this smaller amount of air, the risk of thermal oxidation is also limited. Furthermore, a powder with a significantly improved density contributes to improving the strength of the bed of powder in laser sintering. Finally, the transportation and handling of the powder are thereby facilitated.

[0033] The following examples illustrate in a non-limiting manner the scope of the invention:

Example 1: Density Measurement

[0034] The tapped density and non-tapped density are measured according to ISO standard 1068-1975 (F) in the following way: [0035] introduce a volume of powder into a graduated 250 ml glass measuring cylinder; [0036] level, if necessary, the free surface of the powder without tapping it and note the volume V0; [0037] weigh the cylinder with the powder with a 0.1 g precision balance which has been tared beforehand; [0038] place the cylinder on the plate of the tapping apparatus of the STAV 2003 type; [0039] tap with 1250 drops, note the volume V1; [0040] tap with 1250 drops, note the volume V2; [0041] repeat the tapping operation until two equivalent volumes Vi are obtained. Note Vf corresponding to the identical volumes Vi.

[0042] The non-tapped density is the weight of product introduced divided by V0. The tapped density is the weight of powder introduced divided by Vf. The tapped and non-tapped densities are both expressed in kg/m.sup.3.

Example 2: Densification of a PEKK Powder by Means of the Process which is the Subject of the Invention

[0043] A PEKK powder sold under the reference KEPSTAN® 6002 by the company Arkema, containing 60% of terephthalic units relative to the sum of the terephthalic and isophthalic units, the particle size of which has a dv50 of 50 μm plus or minus 5 μm, and the tapped density of which is 320 kg/m.sup.3, is subjected to various thermomechanical treatments in a Henschel rapid mixer, the blade-tip speed of which is about 43 m/s.

[0044] The Dv50, or median volume diameter, corresponds to the value of the particle size which divides the particle population examined exactly in two. The Dv50 is measured according to standard ISO9276—parts 1 to 6. In the present description, a Malvern Mastersizer 2000 particle size analyser is used, and the measurement is carried out via the liquid process by powder laser diffraction.

[0045] Three samples of powder are compared with the initial powder. The curve of density, as a function of the thermomechanical treatment and of time, obtained for these three samples is represented in FIG. 1 and the results obtained are collated in Table I below.

TABLE-US-00001 TABLE I Treatment time Tapped density Gain in (min) (in kg/m.sup.3) density Initial powder 320 E1: Henschel, without 45 500 56% cooling E2: Henschel, with cooling 60 390 22% E3: E2 in Henschel, 30 480 50% without cooling

[0046] A first sample of powder, referenced E1, the curve of which is represented as a continuous black line in FIG. 1, was mixed in the rapid mixer without thermal regulation, i.e. without cooling. The gain in tapped density is 56% compared with the initial powder after 45 minutes.

[0047] A second sample of powder, referenced E2, the curve of which is represented as discontinuous lines in FIG. 1, was mixed in the rapid mixer with thermal regulation, i.e. with cooling to an ambient temperature of about 25° C. In this case, the gain in tapped density is 22% compared with the initial powder after 60 minutes and increases further as a function of the mixing time, to reach 28% after 120 minutes of mixing.

[0048] A third sample of powder, referenced E3, the curve of which is represented as a grey continuous line in FIG. 1, corresponding to the powder of the sample E2 obtained after thermally regulated mechanical treatment, was mixed in the rapid mixer without thermal regulation. The gain in tapped density is 50% compared with the initial powder after 30 minutes, and 23% compared with the powder of the second sample E2 mixed with thermal regulation.

[0049] These examples demonstrate that the densification is strongly influenced not only by the mechanical stress applied to the powder, but also by the temperature, even if the latter remains modest compared with the heat treatments carried out thus far on the powders.