METHOD FOR THE THERMAL TREATMENT OF POLY-ARYLENE ETHER KETONE KETONE POWDERS SUITABLE FOR LASER SINTERING

Abstract

The invention relates to a process for the heat treatment of poly(arylene ether ketone ketone) powder suitable for laser sintering, and also to the powders resulting from this process.

Claims

1. A process for the treatment of a powder comprising PEKK to obtain a treated powder, wherein the treated powder has a measured flowability exhibiting a passage time in a 17 mm funnel of less than 40 s, limit included, said flowability being measured in the following way: a glass funnel with an orifice of 17 mm is filled with the treated powder up to 5 mm from the edge and the orifice of the bottom is blocked with a finger, the flow time of the treated powder is measured with a stopwatch, if flow does not take place, the funnel is tapped using a spatula, wherein the operation is repeated, if required, the flow time and the number of tapped blows using the spatula are recorded, the process comprising the following stages: arranging the powder comprising PEKK in a ventilated chamber or any other heating system; heating the powder comprising PEKK at a temperature of between T10 C. and T+10 C., where T=3.75*A+37.5, expressed in C., A representing the percentage by weight of terephthalic unit with respect to the sum of the terephthalic and isophthalic units of between 55% and 85%, and for a time strictly of less than 30 minutes.

2. The process as claimed in claim 1, wherein, in addition to the PEKK, the powder comprises a PEK, PEEKEK, PEEK or PEKEKK powder in proportions by weight such that the PEEK represents more than 50%.

3. The process as claimed in claim 1, wherein the powder additionally comprises a filler.

4. The process as claimed in claim 1, wherein the powder additionally comprises at least one additive.

5. The process as claimed in claim 1, wherein the ventilated chamber is a static oven.

6. The process as claimed in claim 1, wherein the ventilated chamber is a fluidized bed.

7. The process as claimed in claim 1, wherein the ventilated chamber is a tube in which hot air and the powder circulate countercurrentwise.

8. The process as claimed in claim 5, wherein the residence time is greater than 15 minutes but less than 30 minutes.

9. The process as claimed in claim 6, wherein the residence time is greater than 2 minutes but less than 30 minutes.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0021] The poly(arylene ether ketone ketone)s used in the invention comprise units of formula IA, of formula IB and their mixture.

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[0022] In a more general context, the poly(arylene ether ketone ketone)s corresponding to the generic names PEK, PEEKEK, PEEK or PEKEKK (where E denotes an ether functional group and K a ketone functional group) cannot be excluded, in particular when their use takes place in a way combined with that of the PEKK in proportions where the PEKK represents more than 50% in proportions by weight and preferably more than 80% in proportions by weight, limits included.

[0023] Preferably, the poly(arylene ether ketone ketone)s are poly(ether ketone ketone)s comprising a mixture of IA and IB units, so that the percentage by weight of terephthalic units with respect to the sum of the terephthalic and isophthalic units is between 55% and 85% and preferably between 55% and 70%, ideally 60%. Terephthalic and isophthalic unit is understood to mean the formula of terephthalic acid and isophthalic acid respectively.

[0024] These poly(arylene ether ketone ketone)s are provided in the form of powders which may have been prepared by milling or precipitation.

[0025] They exist, after the heat treatment process of the invention, in the form of a powder, the flowability of which in a 17 mm funnel is less than 40 s, limit included, preferably less than 30 s and more preferably less than 20 s.

[0026] The powders or mixtures of powders used in the process which is a subject matter of the invention can be obtained, for example, by a milling process described in the application FR 1160258. They can, if appropriate, be additivated with or contain different compounds, such as reinforcing fillers, in particular inorganic fillers, such as carbon black, nanotubes, which may or may not be of carbon, fibres, which may or may not be ground, stabilizing agents (light, in particular UV, and heat stabilizing agents), glidants, such as silica, or also optical, brighteners, dyes, pigments or a combination of these fillers and/or additives.

[0027] The process for the treatment of such powders in accordance with the invention and which makes it possible to obtain the powders in accordance with the invention consists in causing the powder to reside in a device held at temperature, typically between a temperature T10 C. and T+10 C., where T=3.75*A+37.5, expressed in C. (A representing the percentage by weight of terephthalic unit with respect to the sum of the terephthalic and isophthalic units and of between 55% and 85% and preferably between 55% and 70%, ideally 60%), preferably between 1-5 C. and T+5 C. and more preferably between T3 C. and T+3 C., ideally T, for times which are strictly less than 30 minutes. This is because it has been observed that the optimum temperature depends on the proportion by weight 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 be departing from the scope of the invention to carry out several successive heat treatments (at the same temperature or at two different temperatures of between T10 C. and T+10 C., where T=3.75*A+37.5, expressed in C., A representing the percentage by weight of terephthalic unit with respect to 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, whereas, in a dynamic heating system, such as a tube in which the powder and a hot gas circulate countercurrentwise or also a heated fluidized bed, a residence time of the order of a few minutes may be sufficient, typically greater than 2 minutes but strictly less than 30 minutes and preferably between 2 and 15 minutes. The treatment can also be carried out in a vane dryer, in a vertical shaft dryer, in a rotary oven or also in a tunnel heated using infrared lamps.

[0028] The powder resulting from this heat treatment is subsequently used in a device for sintering powders under a laser beam in order to make possible the manufacture of an object. The use of such powders in processes such as rotational molding cannot be excluded.

BRIEF DESCRIPTION OF THE DRAWINGS

EXAMPLES

Example 1

Measurement of the Flowability

[0029] The flowability of these powders was carried out in a glass funnel: [0030] A glass funnel with a 17 mm orifice (FIG. 1) is filled with the powder up to 5 mm from the edge. The orifice of the bottom is blocked with a finger. [0031] The flow time of the powder is measured with a stopwatch. [0032] If flow does not take place, the funnel is tapped using a spatula. The operation is repeated, if required. [0033] The flow time and the number of tapped blows using the spatula are recorded.

Example 2

[0034] A Kepstan 6003 powder from Arkema, containing 60% of terephthalic units with respect to the sum of the terephthalic and isophthalic units, the particle size of which exhibits a dv50 of 50 m plus or minus 5 m, is subjected to a heat treatment of 260 C. in a crystallizing dish in a ventilated oven. The powder is arranged in a crystallizing dish so that the thickness of the powder bed is between 1 and 1.5 cm.

[0035] After treatment, the powders were sieved on a 250 m vibrating sieve in order to deagglomerate them.

[0036] The Dv50 referred to here is the median diameter by volume, which corresponds to the value of the particle size which divides the population of particles examined exactly into two. The Dv50 is measured according to the standard ISO 9276 -parts 1 to 6. In the present description, a Malvern particle sizer, Mastersizer 2000, is used and the measurement is carried out by the liquid route by laser diffraction on the powder.

[0037] The results are given in table 1 for residence times varying from 15 minutes to 25 minutes.

TABLE-US-00001 TABLE 1 Kepstan 6003PL 15 min at 25 min at untreated 260 C. 260 C. Flowability, Time (s) 48 35 17 17 mm funnel Number of blows multi multi 10

[0038] It is found that the flowability is improved from 15 min of heat treatment (flow in 35 s versus 48 s). A heat treatment of 25 min very significantly improves the flowability of the powder.

[0039] The term multi is employed when tapping on the funnel is continuous.