Method for preparing polyphenylene sulfide polymer particles

Abstract

The present invention relates to a method for preparing polyphenylene sulfide polymer (PPS) particles based on the use of a polyester polymer (PE) containing units derived from a dicarboxylic acid component and a diol component, wherein at least 2 mol% of the diol component is a poly(alkylene glycol). The method involves melt-blending the PPS and PE, cooling the blend, and recovering the particles by dissolving the PE in water. The present invention relates to the resulting PPS particles and their use in SLS 3D printing, coatings, and the reinforcement of thermosets. [Selected Figure] Figure 1

Description

[Technical field]

[0001] Related Applications This application claims priority to U.S. Provisional Patent Application No. 62 / 516,387, filed June 7, 2017, and European Patent Application No. 17184614.0, filed August 3, 2017, the entire contents of each of which are incorporated herein by reference for all purposes.

[0002] The present invention relates to a method for preparing polyphenylene sulfide polymer (PPS) particles based on the use of a polyester polymer (PE) containing units derived from a dicarboxylic acid component and a diol component, where at least 2 mol% of the diol component is a poly(alkylene glycol). The method comprises melt blending PPS and PE, cooling the blend, and recovering the particles by dissolving the PE in water. The present invention also relates to the PPS particles obtained therefrom and the use of these particles in SLS 3D printing, coating, and reinforcement of thermosets. [Background technology]

[0003] Additive manufacturing systems are used to print or build 3D objects from digital blueprints created with computer-aided design (CAD) modeling software. Selective laser sintering ("SLS"), one available additive manufacturing technology, uses electromagnetic radiation from a laser to fuse powdered material into a mass. The laser selectively fuses the powdered material by scanning a cross-section generated from the digital blueprint of the object on the surface of the powder bed. After the cross-section is scanned, the powder bed is lowered one layer thickness, a new layer of material is applied, and the bed is rescanned. Localized full coalescence of the polymer particles in the top powder layer is required, as well as adhesion with the previous sintered layer. This process is repeated until the object is completed.

[0004] Schmid et al. (J. Mater. Res,Vol 29,No.17,2014) provides an overview of the properties of polymers and their powder morphologies for SLS 3D printing. The particles need to be spherical to facilitate free-flowing behavior and to be distributed evenly in the printer's powder bed by a roller or blade system. Generally, spherical particles with a particle size distribution of 20-80 μm work best on SLS machines.

[0005] Spherical polymer powders can be prepared by a process called prilling, in which the polymer is dissolved in an organic solvent and subsequently precipitated into a large volume of a non-solvent. First, the use of a solvent creates significant environmental and waste disposal issues. Second, the process requires that the polymer be soluble in the organic solvent at a level sufficient for efficient processing. Although polyphenylene sulfide (PPS) exhibits beneficial thermal, mechanical, and chemical resistance properties that make it particularly interesting for SLS 3D printing, PPS is insoluble in most common solvents.

[0006] U.S. Patent No. 8,454,866 B2 discloses the preparation of aliphatic polyamide powders by forming melt blends with additives that are block copolymers containing poly(alkylene oxide) blocks. These blends disintegrate in water to produce a dispersion of polyamide particles that can then be separated by filtration and drying. The poly(alkylene oxide) polymers described in this patent, while useful for preparing aliphatic polyamide powders, lack the thermal stability for use with high performance aromatic polymers.

[0007] JP2014-043522 describes the use of modified PET melt-blended with PPS to prepare PPS particles. However, the modified PET does not dissolve in water heated up to 95°C.

[0008] One of the objects of the present invention is to provide a method for preparing spherical PPS particles without using organic solvents.

[0009] Another object of the present invention is to provide PPS particles that are well suited for SLS 3D printing, coating compositions, and reinforcement of thermosets. [Brief description of the drawings]

[0010] [Figure 1] 1 is a scanning electron microscope (SEM) image of the PPS particles of Example 1. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0011] The first object of the present invention is a method for preparing spherical PPS particles without using organic solvents. The applicant's achievement is to identify a class of materials, referred to herein as polyester polymers (PE), that have sufficient thermal stability for melt blending with PPS, allowing the preparation of spherical PPS particles suitable for processing with high-temperature aromatic PPS polymers. The PE polymers of the present invention are resistant to high temperatures, i.e., they do not degrade at high temperatures, especially above 250°C. Furthermore, the polyester polymers (PE) can be dissolved in water, possibly heated to temperatures up to 95°C, without the need to add water containing a base or acid. Thus, the PE polymers of the present invention not only exhibit sufficient thermal stability for melt blending with PPS, but are also water-soluble or water-dispersible, which makes them easy to over-process for the preparation of PPS particles.

[0012] The process of the present invention is based on melt blending PPS with a water-soluble or water-dispersible polyester (PE) to form PPS particles dispersed in a phase made of the water-soluble or water-dispersible polyester (PE), e.g., by adding sufficient energy to form discrete particles. The blend is then cooled and the particles are recovered by dissolving the polyester in water (optionally heated to a temperature of up to 95° C.).

[0013] In this application: - any description, even if made in relation to a particular embodiment, is applicable to and interchangeable with other embodiments of the present disclosure; - when an element or component is said to be included in and / or selected from a list of enumerated elements or components, it is to be understood that in the relevant embodiments expressly contemplated herein, the element or component may also be any one of the individual enumerated elements or components, or may be selected from a group consisting of any two or more of the explicitly enumerated elements or components, and that any element or component enumerated in a list of elements or components may be omitted from such list; - any recitation herein of numerical ranges by endpoints includes all numbers subsumed within the recited range, as well as the endpoints of the range and equivalents.

[0014] More precisely, the present invention relates to - a) at least one PPS; b) at least one dicarboxylic acid component, At least one diol component, at least 2 mol % of which is a diol component of formula (I): H(OC m H 2m ) n -OH (wherein m is an integer from 2 to 4, and n varies from 2 to 10). a diol component which is a poly(alkylene glycol) having the formula: At least one polyester polymer (PE) containing units derived from melt blending a mixture (M) containing - processing the mixture (M) into pellets or strands; - optionally cooling the pellets or strands to a temperature below 80°C; - contacting the pellets or strands with water, for example by immersing said pellets or strands in water which has optionally been heated to a temperature of up to 95°C; - Recovering the particles, for example by separating them from the water; - optionally drying the particles; and - optionally sieving the particles; The present invention relates to a method for preparing polyphenylene sulfide polymer (PPS) particles, comprising:

[0015] More generally, the process consisting of melt blending the mixture (M) can be carried out using any suitable equipment, such as an endless screw mixer or a stirrer mixer, e.g. a kneader, that is compatible with the temperature required to melt the aromatic PPS polymer. The amount of energy added to this process can be adjusted to control the size of the polymer particles obtained therefrom. The person skilled in the art can adjust the equipment (e.g. the screw geometry) and the equipment parameters (e.g. the rotation speed) to obtain particles of the desired size, for example with an average diameter varying between about 0.5 μm and about 500 μm.

[0016] According to a preferred embodiment, the melt blending step is carried out at a temperature above 280°C, such as above 290°C, above 300°C, or above 310°C.

[0017] The step of processing the mixture into pellets or strands can be carried out by a process of extrusion through a die.

[0018] The steps of melt blending and processing into pellets or strands are preferably carried out in an extruder equipped with an extrusion die.

[0019] The cooling step is carried out by any suitable means, at a temperature below 80° C., for example below 50° C., and may in particular be air cooling or quenching in a liquid, for example in water.

[0020] The step of contacting the pellets or strands with water may consist of immersing them in water, possibly in multiple water baths, for example water heated to a temperature of up to 95° C. This allows the polyester to be dissolved and the PPS particles to be recovered. The inventors have demonstrated that it is not necessary to add an acid or base to the water in order to fully dissolve the polyester. The invention advantageously utilizes water or running water of neutral pH.

[0021] The process steps of the present invention may be carried out batchwise or continuously.

[0022] According to one embodiment, the steps of cooling the pellets or strands at a temperature below 80° C., e.g. below 50° C., and contacting the pellets or strands with water, e.g. by immersing the pellets or strands in water (which may optionally be heated to a temperature of up to 95° C.), can be carried out simultaneously in the same equipment.

[0023] The process of the invention may also comprise the additional step of drying the particles and / or sieving the particles. The drying step may be carried out, for example, in a fluidized bed.

[0024] Polyphenylene Sulfide Polymer (PPS) According to the present invention, a "polyphenylene sulfide polymer (PPS)" is a polymer in which at least about 50 mol % of its repeating units are repeating units of the formula (L) (R PPS ): means any polymer that is TIFF0007608053000001.tif32161, During the ceremony, - Each R is a hydrogen atom, a halogen atom, or a C1-C 12 Alkyl groups, C7-C 24 Alkylaryl group, C7-C 24 Aralkyl groups, C6-C 24 Arylene group, C1-C 12 Alkoxy groups and C6-C 18 aryloxy groups; - i is an integer from 0 to 4.

[0025] In its broadest definition, the polyphenylene sulfide polymers (PPS) of the present invention can be comprised of substituted and / or unsubstituted phenylene sulfide groups.

[0026] According to one embodiment of the present invention, the polyphenylene sulfide polymer (PPS) has at least 50 mol % of its repeating units being repeating units of formula (L') (R PPS ): TIFF0007608053000002.tif32161, and refers to any polymer in which R1 is a hydrogen atom.

[0027] According to one embodiment of the present invention, the polyphenylene sulfide polymer is a polymer in which at least about 60 mol%, at least about 70 mol%, at least about 80 mol%, at least about 90 mol%, at least about 95 mol%, at least about 99 mol% of the repeat units in the PPS are repeat units (R PPS ) is a polymer such that

[0028] The mole % herein is based on the total moles in the PPS.

[0029] According to one embodiment of the present invention, the PPS polymer has about 100 mol % of the repeat units being repeat units of formula (L) or (L′) (R PPS According to this embodiment, the PPS polymer is essentially a polymer having repeat units (R PPS )

[0030] PPS is manufactured by, among others, Solvay Specialty Polymers USA, LLC. and sold under the trade name Ryton® PPS.

[0031] According to the present invention, the melt flow rate of PPS (at 316° C. under a weight of 5 kg according to ASTM D1238 procedure B) may be from 50 to 400 g / 10 min, for example from 60 to 300 g / 10 min or from 70 to 200 g / 10 min.

[0032] According to one embodiment, the PPS polymer is present in mixture (M) in an amount of less than 60 wt.%, less than 55 wt.%, less than 50 wt.%, less than 45 wt.%, less than 40 wt.%, less than 35 wt.%, less than 30 wt.%, less than 25 wt.%, or less than 20 wt.%, based on the total weight of mixture (M).

[0033] Polyester Polymer (PE) According to the present invention, "polyester polymer (PE)" is at least one dicarboxylic acid component, at least one diol component, at least 2 mol % of which is of formula (I): H(OC m H 2m ) n -OH (wherein m is an integer from 2 to 4, and n varies from 2 to 10). a diol component which is a poly(alkylene glycol) of the formula: By "polymer" is meant any polymer containing units derived therefrom.

[0034] According to one embodiment, the dicarboxylic acid component comprises at least one aromatic dicarboxylic acid selected from the group consisting of, for example, isophthalic acid (IPA), terephthalic acid (TPA), naphthalenedicarboxylic acid (e.g., naphthalene-2,6-dicarboxylic acid), 4,4'-dibenzoic acid, 2,5-pyridinedicarboxylic acid, 2,4-pyridinedicarboxylic acid, 3,5-pyridinedicarboxylic acid, 2,2-bis(4-carboxyphenyl)propane, bis(4-carboxyphenyl)methane, 2,2-bis(4-carboxyphenyl)hexafluoropropane, 2,2-bis(4-carboxyphenyl)ketone, 4,4'-bis(4-carboxyphenyl)sulfone, 2,2-bis(3-carboxyphenyl)propane, bis(3-carboxyphenyl)methane, 2,2-bis(3-carboxyphenyl)hexafluoropropane, 2,2-bis(3-carboxyphenyl)ketone, bis(3-carboxyphenoxy)benzene, and mixtures thereof.

[0035] According to one embodiment, the diol component has at least 2 mol % of the diol component represented by formula (II): H(O-CH2-CH2) n -OH (n varies from 2 to 10) It is a poly(ethylene glycol).

[0036] According to one embodiment, the diol component has at least 4 mol%, at least 10 mol%, at least 20 mol%, at least 30 mol%, at least 40 mol%, or at least 50 mol% of the diol component (based on the total number of moles of the diol component) represented by formula (I): H(OC m H 2m ) n -OH (m is an integer between 2 and 4, and n ranges from 2 to 10) and preferably a poly(alkylene glycol) of the formula (II): H(O-CH2-CH2) n -OH (n varies from 2 to 10) It is a poly(ethylene glycol).

[0037] According to another embodiment, the diol component is such that at least 2 mol%, at least 4 mol%, at least 10 mol%, at least 20 mol%, at least 30 mol%, at least 40 mol%, or at least 50 mol% of the diol component (based on the total number of moles of the diol component) is diethylene glycol of formula HO-CH-CH-O-CH-CH-OH.

[0038] According to a further embodiment, apart from the 2 mol % minimum content of poly(alkylene glycol), the diol component may comprise at least one diol selected from the group consisting of ethylene glycol, 1,4-cyclohexanedimethanol, propane-1,2-diol, 2,2-dimethyl-1,3-propanediol, 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 2-methyl-1,5-pentanediol, isosorbide, and 2,5-bishydroxymethyltetrahydrofuran.

[0039] According to another embodiment, the diol component of the polyester polymer (PE) is diols selected from the group consisting of ethylene glycol, 1,4-cyclohexanedimethanol, propane-1,2-diol, 2,2-dimethyl-1,3-propanediol, 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 2-methyl-1,5-pentanediol, isosorbide, and 2,5-bishydroxymethyltetrahydrofuran; at least 2 mol % of poly(ethylene glycol) of formula (I): H(O-CH2-CH2) n -OH (n varies from 2 to 10). It essentially consists of:

[0040] According to another embodiment, the diol component of the polyester polymer (PE) is diols selected from the group consisting of ethylene glycol, 1,4-cyclohexanedimethanol, propane-1,2-diol, 2,2-dimethyl-1,3-propanediol, 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 2-methyl-1,5-pentanediol, isosorbide, and 2,5-bishydroxymethyltetrahydrofuran; at least 2 mole % diethylene glycol (based on the total moles of the diol component); It essentially consists of:

[0041] According to the present invention, preferred polyesters (PE) are polyesters further comprising repeat units derived from a difunctional monomer comprising at least one SO3M group attached to an aromatic nucleus, the functional group being carboxy, M being H or a metal ion selected from the group consisting of sodium, potassium, calcium, lithium, magnesium, silver, aluminum, zinc, nickel, copper, palladium, iron and cesium, preferably a metal ion selected from the group consisting of sodium, lithium and potassium. Such preferred polyesters may also be referred to as sulfopolyesters (SPEs). According to this embodiment, the difunctional sulfomonomer may be present in the SPE in a molar ratio comprised, for example, between 1 and 40 mol %, for example between 5 and 35 mol %, or between 8 and 30 mol %, based on the total moles in the SPE (i.e., the total moles of diacid and diol components when the SPE is composed only of diacid and diol components).

[0042] According to one embodiment of the present invention, the polyester (PE) is at least one dicarboxylic acid component, at least one diol component, at least 2 mol % of which is of formula (I): H(OC m H 2m ) n -OH (m is an integer from 2 to 4, n ranges from 2 to 10, preferably m is equal to 2 and n is equal to 2). a diol component which is a poly(alkylene glycol) of the formula: - at least one bifunctional monomer comprising at least one SO3M group attached to an aromatic nucleus, the functional group being carboxy and M being H or a metal ion selected from the group consisting of sodium, lithium and potassium; Includes units of origin.

[0043] According to another embodiment of the present invention, the polyester (PE) is at least one aromatic dicarboxylic acid component, at least one diol component, at least 1 mol % (based on the total number of moles of units in the PE, e.g. the total number of moles of diacid and diol components when the PE is composed only of diacid and diol units) of formula (I): H(OC m H 2m ) n -OH (m is an integer between 2 and 4, and n ranges from 2 to 10) poly(alkylene glycol), at least one aromatic dicarboxylic acid containing at least one SO3M group attached to the aromatic nucleus, where M is H or a metal ion selected from the group consisting of sodium, lithium and potassium, Includes units of origin.

[0044] According to a preferred embodiment of the present invention, the polyester polymer (PE) is aromatic dicarboxylic acids selected from the group consisting of isophthalic acid (IPA), terephthalic acid (TPA), naphthalenedicarboxylic acids (for example naphthalene-2,6-dicarboxylic acid), 4,4'-dibenzoic acid, 2,5-pyridinedicarboxylic acid, 2,4-pyridinedicarboxylic acid, 3,5-pyridinedicarboxylic acid, 2,2-bis(4-carboxyphenyl)propane, bis(4-carboxyphenyl)methane, 2,2-bis(4-carboxyphenyl)hexafluoropropane, 2,2-bis(4-carboxyphenyl)ketone, 4,4'-bis(4-carboxyphenyl)sulfone, 2,2-bis(3-carboxyphenyl)propane, bis(3-carboxyphenyl)methane, 2,2-bis(3-carboxyphenyl)hexafluoropropane, 2,2-bis(3-carboxyphenyl)ketone, bis(3-carboxyphenyl)benzene, and mixtures thereof, preferably isophthalic acid, diols selected from the group consisting of ethylene glycol, 1,4-cyclohexanedimethanol, propane-1,2-diol, 2,2-dimethyl-1,3-propanediol, and mixtures thereof; - at least 1 mole % (based on the total moles of units in the PE, e.g. the total moles of diacid and diol components if the PE is composed only of diacid and diol units) of diethylene glycol; - aromatic dicarboxylic acids containing at least one SO3M group attached to the aromatic nucleus (for example isophthalic acid, terephthalic acid, 2,6-naphthalenedicarboxylic acid), where M is H or a metal ion selected from the group consisting of sodium, lithium and potassium; It may comprise or consist essentially of units derived from

[0045] According to one embodiment, the PE comprises at least 2 mol%, at least 4 mol%, at least 10 mol%, at least 20 mol%, at least 30 mol%, at least 40 mol%, or at least 50 mol% diethylene glycol, based on the total moles of units in the PE (e.g., the total moles of diacid and diol components when the PE is composed only of diacid and diol units).

[0046] Illustrative of such polyesters are Eastman AQ Polymers, particularly those having glass transition temperatures in the range of about 25° C. to about 50° C. Most preferred is Eastman AQ 38S, a polyester composed of diethylene glycol, cyclohexanedimethanol / (CHDM), isophthalate, and sulfoisophthalate units.

[0047] The polyester (PE) of the present invention is in the form of a salt of sulfonic acid or / and carboxylic acid, more precisely sulfonate-SO3 - , or carboxylate-COO - Therefore, the PE may have one or more groups (SO3 - M + ) and / or (COO - M + ) wherein M is a metal. According to one embodiment, M is selected from the group consisting of sodium, potassium or lithium, calcium, magnesium, silver, aluminum, zinc, nickel, copper, palladium, iron, and cesium.

[0048] The polyester (PE) of the present invention may be derived, for example, by esterification of the components mentioned above.

[0049] The number average molecular weight of the polyester (PE) determined by GPC may be from 1,000 g / mol to 40,000 g / mol, more preferably from 2,000 g / mol to 30,000 g / mol.

[0050] According to one embodiment, the PE polymer is present in mixture (M) in an amount of at least 30% by weight, at least 35% by weight, at least 40% by weight, at least 45% by weight, at least 50% by weight, at least 55% by weight, at least 60% by weight, at least 65% by weight, at least 70% by weight, at least 75% by weight, or at least 80% by weight, based on the total weight of mixture (M).

[0051] PPS particles The method of the present invention allows the preparation of PPS particles of regular shape and size.

[0052] As used herein, the term "particle" refers to an individualized entity.

[0053] The particles may have an average diameter of less than about 200 μm, in some embodiments from about 0.5 μm to about 150 μm, or from about 1 μm to about 100 μm, or from about 1 μm to about 50 μm. The average diameter can be assessed by scanning electron microscopy (SEM).

[0054] The particles of the present invention can be characterized by their particle size distribution D50 (abbreviated "D50"), also known as the median diameter or middle value of the particle size distribution, according to which 50% of the particles in a sample are larger and 50% of the particles in a sample are smaller. Particle size analysis can be performed, for example, using a Microtrac Sample Delivery Controller (SDC) equipped with a Microtrac Sample Delivery Controller (SDC). TM This can be done with the S3500.

[0055] According to one embodiment of the invention, the PPS particles have a D50 comprised between 5 μm and 100 μm, for example between less than 80 μm and more than 10 μm or between less than 60 μm and more than 15 μm.

[0056] The particles of the present invention can be characterized by their bulk density and their tapped density. The bulk density of a powder is the ratio of the mass of a powder sample in the untapped state to its volume, including the contribution of the interparticle void volume. Bulk density is expressed in grams per milliliter (g / ml) or grams per cubic centimeter (g / cm 3 ) Density measurements can be performed using a Quantachrome Autotap TM This can be done with a tap density analyzer.

[0057] According to one embodiment of the invention, the PPS particles are a bulk density of at least 0.45, preferably at least 0.47, more preferably at least 0.49, and a tap density of at least 0.55, preferably at least 0.57, more preferably at least 0.59; has.

[0058] The present invention relates to - P.P.S. at least one dicarboxylic acid component, At least one diol component, at least 2 mol % of which is a diol component of formula (I): H(OC m H 2m ) n -OH (wherein m is an integer from 2 to 4, and n varies from 2 to 10). and a diol component which is a poly(alkylene glycol) having the formula: melt blending with at least one polyester polymer (PE) containing units derived from - Dispersing PE in water; The present invention also relates to polyphenylene sulfide polymer (PPS) particles produced by a process comprising:

[0059] All of the above-mentioned embodiments relating to the method of preparation of polyphenylene sulfide polymer (PPS) particles equally apply to this section of the present specification.

[0060] The following possible steps may be carried out on the particles of PPS obtained from the above-mentioned method: - coating with a powder flow enhancer such as an inorganic material, e.g. silica; - drying at a temperature of at least 80°C, for example at least 90°C, for at least 0.5 hours, preferably at least 1 hour, optionally under reduced pressure; and - sieving process; At least one of the following may be performed.

[0061] The particles of the invention may be substantially spherical, for example having a circularity and / or roundness of at least 0.75, such as at least 0.8 or at least 0.85.

[0062] Circularity is defined as a measure of the surface smoothness of a particle and is measured according to the following formula: TIFF0007608053000003.tif18161

[0063] Circularity is defined as a measure of the sphericity of a particle and is measured according to the following formula: TIFF0007608053000004.tif21161

[0064] The present invention also relates to blends of the polyphenylene sulfide polymer (PPS) particles of the present invention, and to methods for preparing such blends.

[0065] According to one embodiment, the blend of PPS particles of the invention comprises at least two populations of particles having a D50 in the range of 5 to 100 μm, preferably 8 to 90 μm, and more preferably 10 to 70 μm.

[0066] Optional ingredients The particles of the present invention may contain various additives such as lubricants, heat stabilizers, light stabilizers, antioxidants, pigments, processing aids, dyes, or fillers (e.g. biocompatible fillers such as hydroxyapatite). For example, titanium dioxide, zinc oxide, cerium oxide, silica, or zinc sulfide may be mentioned in particular, which are used as lubricants and / or abrasives. The fillers (e.g. reinforcing or mineral fillers) may be selected from the group consisting of glass fibers, carbon fibers, talc, wollastonite, calcium carbonate, mica, etc.

[0067] The polymeric composition may further include flame retardants, such as halogenated and halogen-free flame retardants.

[0068] One of the main advantages of the present invention is that the optional additives, if present, are located inside the PPS particles and uniformly distributed throughout the polymeric material.

[0069] Purpose The particles of the present invention can be used in a variety of applications, particularly in SLS 3D printing, coatings, and reinforcement of thermosets.

[0070] Therefore, the present invention also relates to the use of PPS particles for the production of three-dimensional objects using a laser sintering additive manufacturing system. EXAMPLES

[0071] Example 1 raw materials PPS: Ryton® QC160N available from Solvay Specialty Polymers USA, LLC

[0072] PE: Eastman AQ, a sulfopolyester available from Eastman TM 48. This PE is composed of diethylene glycol, cyclohexanedimethanol (CHDM), isophthalate, and sulfoisophthalate units. 1H NMR analysis shows that the molar concentration of diethylene glycol is 70 mol % based on the total moles of diol (CHMD + diethylene glycol).

[0073] PTS: Para-Toluene Sulfonic Acid Ester from Spectrum Chemical

[0074] Material Processing The blends were prepared according to Table 1. 15 g of each composition was melt blended in a DSM Xplore® Micro-Compounder at the specified temperature (see Table 1) and 150-200 rpm for 3 minutes. Each blend was then processed into strands and then quenched until solidified. The samples were immersed in water heated to 95°C for 2 hours. The water was then removed. The samples were again immersed in water heated to 90°C for 2 hours.

[0075] Some compositions (Example 1, Example 2, and Example 3) gave polymer powders according to the invention, which were then isolated by filtration and dried in vacuum.

[0076] TIFF0007608053000005.tif66170

[0077] Scanning Electron Microscope (SEM) Each polymer sample was examined using a scanning electron microscope as shown below. Powders were dispersed onto carbon tape fixed to an aluminum stub and sputter coated with AuPd using an Emitech K575x Turbo sputter coater. Images were recorded using a Hitachi S-4300 cold cathode field emission scanning electron microscope and the images were analyzed for average diameter using ImageJ v 1.49b Java-based image analysis software for an approximate set of 50 particle images. A summary of the average particle sizes estimated from the SEM photographs of the powders is shown in Table 2.

[0078] FIG. 1 is a SEM scan of the PPS particles of Example 1.

[0079] Particle Size Analysis-D50 Particle size analysis (PSA) was performed using a Microtrac S3500 equipped with a Microtrac Sample Delivery Controller (SDC).

[0080] TIFF0007608053000006.tif65170

[0081] Example 2 This example is intended to demonstrate that the modified PET components described in JP2014-043522A are not soluble in water heated to a temperature of 95°C.

[0082] raw materials PET: Estar® polyester EN052 available from Eastman Chemical

[0083] DMSI: Dimethyl 5-sulfoisophthalate sodium salt (98% purity, Mw: 296.23) commercially available from Alfa Aesar

[0084] Method for preparing modified PET 13 g of PET (90 mol%) and 2.3 g of DMSI (10 mol%) were melt blended in a DSM microcompounder at 310° C. for 4-8 min.

[0085] Water Solubility Test All samples were exposed to a water bath heated to 80° C. for 1 hour with 0.5 g of material and 10 g of deionized water.

[0086] TIFF0007608053000007.tif57170

[0087] Example 3 raw materials PPS: Ryton® QC160N available from Solvay Specialty Polymers USA, LLC.

[0088] PE: Eastman AQ, a sulfopolyester available from Eastman TM 38S. This PE is composed of diethylene glycol, cyclohexanedimethanol (CHDM), isophthalate, and sulfoisophthalate units. 1H NMR analysis shows that the molar concentration of diethylene glycol is 80 mol % based on the total moles of diol (CHMD + diethylene glycol).

[0089] Material Processing The blends were prepared according to Table 4. Each composition was melt blended in a ZSK-26 twin screw extruder (Coperion) at the specific conditions shown in Table 4. Each polymer melt was dripped from the extruder die into a bucket of hot water (60°C) with occasional mixing. The powder was isolated by vacuum filtration using a Buchner funnel. The powder was then washed with 2-3 L of deionized water in the Buchner funnel. The powder was dried under vacuum at 100°C. Each polymer was mixed with colloidal silica (Aerosil® 200, Spectrum Chemical) to obtain a 1 wt% mixture.

[0090] TIFF0007608053000008.tif51170

[0091] Particle Size Analysis-D50 Particle size analysis (PSA) was performed using a Microtrac S3500 equipped with a Microtrac Sample Delivery Controller (SDC).

[0092] Bulk density and tapped density Density is measured using a Quantachrome Autotap with a cycle of 500 taps. TM This was done using a tap density analyzer. TIFF0007608053000009.tif42170

Claims

1. A method for preparing polyphenylene sulfide polymer (PPS) particles, comprising: － a) at least one PPS; b) at least one polyester polymer (PE), at least one aromatic dicarboxylic acid component; At least one diol component, at least 2 mol % of said diol component being of formula (I): H(O-C ｍ H ２ｍ ) ｎ -OH where m is an integer from 2 to 4 and n varies from 2 to 10. a diol component which is a poly(alkylene glycol) having the formula: at least one aromatic dicarboxylic acid containing at least one SO 3 M group attached to the aromatic nucleus, where M is H or a metal ion selected from the group consisting of sodium, lithium and potassium; At least one polyester polymer (PE) comprising units derived from melt blending a mixture (M) containing - processing said mixture (M) into pellets or strands; - cooling the pellets or strands to a temperature below 80°C; - contacting said pellets or strands with water, optionally heated to a temperature of up to 95°C; - recovering said particles; - optionally drying said particles; and - optionally sieving said particles; Including, A method for preparing polyphenylene sulfide polymer (PPS) particles, wherein said at least one polyester polymer (PE) is water-soluble or water-dispersible.

2. At least 50 mol % of the repeating units of the PPS have the formula (L): (In the formula: Each R is a hydrogen atom, a halogen atom, C １ ~C １２ Alkyl group, C ７ ~C ２４ Alkylaryl group, C ７ ~C ２４ Aralkyl group, C ６ ~C ２４ Arylene group, C １ ~C １２ Alkoxy groups, and C ６ ~C １８ aryloxy groups; - i is an integer from 0 to 4. Repeating units (R PPS ): (mol % is based on the total number of moles in the PPS polymer) The method of claim 1, wherein

3. At least 50 mol % of the repeating units of the PPS are represented by the formula (L'): The method according to claim 1 or 2, wherein the repeating unit is (R PPS ).

4. The PE is - isophthalic acid, diols selected from the group consisting of ethylene glycol, 1,4-cyclohexanedimethanol, propane-1,2-diol, 2,2-dimethyl-1,3-propanediol, and mixtures thereof; at least 2 mol % (based on the total number of moles in said PE) of diethylene glycol poly(alkylene glycol); - at least one SO bonded to an aromatic nucleus ３ Aromatic dicarboxylic acids containing an M group, where M is H or a metal ion selected from the group consisting of sodium, lithium, and potassium. The method of any one of claims 1 to 3, comprising or consisting essentially of units derived from:

5. The mixture (M) is a) 10 to 60 wt. % PPS, and b) 40 to 90% by weight of PE The method according to any one of claims 1 to 4, comprising:

6. The method of any one of claims 1 to 5, wherein the melt blending step is carried out at a temperature above 250°C.

Images