Patent Application
20190292690
The present invention relates to the use of a semicrystalline thermoplastic polyester comprising at least one 1,4:3,6-dianhydrohexitol unit which has excellent properties for the production of fibers.
Plastics have become inescapable in the mass production of objects. Indeed, their thermoplastic character enables these materials to be transformed at a high rate into all kinds of objects or articles.
Certain thermoplastic aromatic polyesters have thermal properties which allow them to be used directly for the production of materials. They comprise aliphatic diol and is aromatic diacid units. Among these aromatic polyesters, mention may be made of polyethylene terephthalate (PET), which is a polyester comprising ethylene glycol and terephthalic acid units, used for example in the production of films.
However, for certain applications or under certain usage conditions, it is necessary to improve certain mechanical or else heat-resistance properties. This is why glycol-modified PETs (PETgs) have been developed. They are generally polyesters comprising, in addition to the ethylene glycol and terephthalic acid units, cyclohexanedimethanol (CHDM) units. The introduction of this diol into the PET enables it to adapt the properties to the intended application, for example to improve its impact strength or its optical properties.
Other modified PETs have also been developed by introducing, into the polyester, 1,4:3,6-dianhydrohexitol units, especially isosorbide (PEIT). These modified polyesters have higher glass transition temperatures than the unmodified PETs or the PETgs comprising CHDM. In addition, 1,4:3,6-dianhydrohexitols have the advantage of being able to be obtained from renewable resources such as starch.
Another problem with these PEITs is that they may have insufficient impact strength properties. In addition, the glass transition temperature may be insufficient for the production of certain plastic objects.
In order to improve the mechanical properties of the polyesters, it is known from the prior art to use polyesters in which the crystallinity has been reduced. As regards isosorbide-based polyesters, mention may be made of application US2012/0177854, which describes polyesters comprising terephthalic acid units and diol units comprising from 1 to 60 mol % of isosorbide and from 5 to 99% of 1,4-cyclohexanedimethanol which have improved impact strength properties. As indicated in the introductory section of this application, the aim is to obtain polymers in which the crystallinity is eliminated by the addition of comonomers, and hence in this case by the addition of 1,4-cyclohexanedimethanol. The “Examples” section describes the production of various poly(ethylene-co-1,4-cyclohexanedimethylene-co-isosorbide)terephthalates (PECITs), and gives an example of poly(1,4-cyclohexanedimethylene-co-isosorbide)terephthalate (PCIT).
It may also be noted that while polymers of PECIT type have been the subject of commercial developments, this is not the case for PCITs. Indeed, their production was hitherto considered to be complex, since isosorbide has low reactivity as a secondary diol. Yoon et al. (Synthesis and Characteristics of a Biobased High-Tg Terpolyester of Isosorbide, Ethylene Glycol, and 1,4-Cyclohexane Dimethanol: Effect of Ethylene Glycol as a Chain Linker on Polymerization, Macromolecules, 2013, 46, 7219-7231) thus showed that the synthesis of PCIT is much more difficult to achieve than that of PECIT. This paper describes the study of the influence of the ethylene glycol content on the PECIT production kinetics.
In Yoon et al., an amorphous PCIT (which comprises approximately 29% isosorbide and 71% CHDM, relative to the sum of the diols) is produced to compare its synthesis and its properties with those of PECIT-type polymers. The use of high temperatures during the synthesis induces thermal degradation of the polymer formed if reference is made to the first paragraph of the Synthesis section on page 7222, this degradation especially being linked to the presence of aliphatic cyclic diols such as isosorbide. Therefore, Yoon et al. used a process in which the polycondensation temperature is limited to 270° C. Yoon et al. observed that, even increasing the polymerization time, the process also does not make it possible to obtain a polyester having a sufficient viscosity. Thus, without addition of ethylene glycol, the viscosity of the polyester remains limited, despite the use of prolonged synthesis times.
Thus, despite the modifications made to the PETs, there is still a constant need for novel polyesters having improved properties.
In the plastics field, in particular plastics for the production of fibers, it is necessary to have available a semicrystalline thermoplastic polyester with improved properties which make it possible to obtain fibers that have a better heat resistance and also improved mechanical properties such as elongation at break, rigidity or else persistence.
Objects produced from polymers having terephthalic acid units, ethylene glycol units and isosorbide units and optionally another diol (for example 1,4-cyclohexanedimethanol) are known from document U.S. Pat. No. 6,126,992. All the polymers obtained thus have ethylene glycol units, since it is widely accepted that they are necessary for the incorporation of the isosorbide and to obtaining a high glass transition temperature. Furthermore, the preparation examples implemented make it possible to obtain polymers of which the composition is not entirely satisfactory in fiber production. Indeed, example 1 describes in particular the preparation of a polymer comprising 44% of ethylene glycol unit and 3% of isosorbide unit, i.e. an isosorbide unit/ethylene glycol unit ratio of 0.36, which is not convincing for fiber production.
Document U.S. Pat. No. 6,063,495 describes polyester fibers produced from a polymer having isosorbide units, terephthalic acid units and ethylene glycol units. The fibers thus produced are suitable for commercial or industrial use in the textile industry in particular. However, these polyesters do not have a sufficiently low solution viscosity to be entirely satisfactory in fiber production.
Thus, there is currently still a need to have semicrystalline thermoplastic polyesters containing 1,4:3,6-dianhydrohexitol units for the production of fibers having improved mechanical and thermal properties.
It is thus to the applicant's credit to have found that this object could, against all expectations, be achieved with a semicrystalline thermoplastic polyester based on isosorbide and not having ethylene glycol, while it was hitherto known that the latter was essential for the incorporation of said isosorbide.
Indeed, by virtue of a particular viscosity and a particular ratio of units, the semicrystalline thermoplastic polyester used according to the present invention has improved properties for a use according to the invention in the production of fibers.
Thus, a subject of the invention is the use of a semicrystalline thermoplastic polyester for the production of fibers, said polyester comprising:
A second subject of the invention relates to a process for producing a fiber based on the semicrystalline thermoplastic polyester described above.
Finally, a third subject of the invention relates to a fiber comprising the semicrystalline thermoplastic polyester previously described.
These semicrystalline thermoplastic polyesters of excellent properties and make it possible in particular to produce fibers which have improved mechanical properties.
A first subject of the invention relates to the use of a semicrystalline thermoplastic polyester for the production of fibers, said polyester comprising:
“(A)/[(A)+(B)] molar ratio” is intended to mean the molar ratio of 1,4:3,6-dianhydrohexitol units (A)/sum of 1,4:3,6-dianhydrohexitol units (A) and alicyclic diol units (B) other than 1,4:3,6-dianhydrohexitol units (A).
The term “fibers” as used in the present invention is synonymous with the term filaments and yarns and thus includes continuous or discontinuous monofilaments or multifilaments, non-twisted or intermingled multifilaments, base yarns.
The semicrystalline thermoplastic polyester is free of non-cyclic aliphatic diol units, or comprises a small amount thereof.
“Small molar amount of aliphatic non-cyclic diol units” is intended to mean, especially, a molar amount of aliphatic non-cyclic diol units of less than 5%. According to the invention, this molar amount represents the ratio of the sum of the aliphatic non-cyclic diol units, these units possibly being identical or different, relative to all the monomer units of the polyester.
An aliphatic non-cyclic diol may be a linear or branched aliphatic non-cyclic diol. It may also be a saturated or unsaturated aliphatic non-cyclic diol. Aside from ethylene glycol, the saturated linear aliphatic non-cyclic diol may for example be 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,8-octanediol and/or 1,10-decanediol. As examples of saturated branched aliphatic non-cyclic diol, mention may be made of 2-methyl-1,3-propanediol, 2,2,4-trimethyl-1,3-pentanediol, 2-ethyl-2-butyl-1,3-propanediol, propylene glycol and/or neopentyl glycol. As an example of an unsaturated aliphatic diol, mention may be made, for example, of cis-2-butene-1,4-diol.
This molar amount of aliphatic non-cyclic diol unit is advantageously less than 1%. Preferably, the polyester is free of any aliphatic non-cyclic diol units and more preferentially it is free of ethylene glycol.
Despite the low amount of aliphatic non-cyclic diol, and hence of ethylene glycol, used for the synthesis, a semicrystalline thermoplastic polyester is surprisingly obtained which has a high reduced solution viscosity and in which the isosorbide is particularly well incorporated. Without being bound by any one theory, this would be explained by the fact that the reaction kinetics of ethylene glycol are much faster than those of 1,4:3,6-dianhydrohexitol, which greatly limits the integration of the latter into the polyester. The polyesters resulting therefrom thus have a low degree of integration of 1,4:3,6-dianhydrohexitol and consequently a relatively low glass transition temperature.
The monomer (A) is a 1,4:3,6-dianhydrohexitol and may be isosorbide, isomannide, isoidide, or a mixture thereof. Preferably, the 1,4:3,6-dianhydrohexitol (A) is isosorbide. Isosorbide, isomannide and isoidide may be obtained, respectively, by dehydration of sorbitol, of mannitol and of iditol. As regards isosorbide, it is sold by the applicant under the brand name Polysorb® P.
The alicyclic diol (B) is also referred to as aliphatic and cyclic diol. It is a diol which may especially be chosen from 1,4-cyclohexanedimethanol, 1,2-cyclohexanedimethanol, 1,3-cyclohexanedimethanol or a mixture of these diols. The alicyclic diol (B) is very preferentially 1,4-cyclohexanedimethanol. The alicyclic diol (B) may be in the cis configuration, in the trans configuration, or may be a mixture of diols in the cis and trans configurations.
The molar ratio of 1,4:3,6-dianhydrohexitol units (A)/sum of 1,4:3,6-dianhydrohexitol units (A) and alicyclic diol units (B) other than 1,4:3,6-dianhydrohexitol units (A), i.e. (A)/[(A)+(B)], is at least 0.05 and at most 0.30. Advantageously, this ratio is at least 0.1 and at most 0.28, and more particularly this ratio is at least 0.15 and at most 0.25.
A semicrystalline thermoplastic polyester that is particularly suitable for the production of fibers comprises:
The amounts of different units in the polyester may be determined by 1H NMR or by chromatographic analysis of the mixture of monomers resulting from complete hydrolysis or methanolysis of the polyester, preferably by 1H NMR.
Those skilled in the art can readily find the analysis conditions for determining the amounts of each of the units of the polyester. For example, from an NMR spectrum of a poly(1,4-cyclohexanedimethylene-co-isosorbide terephthalate), the chemical shifts relating to the 1,4-cyclohexanedimethanol are between 0.9 and 2.4 ppm and 4.0 and 4.5 ppm, the chemical shifts relating to the terephthalate ring are between 7.8 and 8.4 ppm and the chemical shifts relating to the isosorbide are between 4.1 and 5.8 ppm. The integration of each signal makes it possible to determine the amount of each unit of the polyester.
The semicrystalline thermoplastic polyesters used according to the invention have a melting point ranging from 210 to 295° C., for example from 240 to 285° C.
Furthermore, the semicrystalline thermoplastic polyesters have a glass transition temperature ranging from 85 to 120° C., for example from 90 to 115° C. The glass transition temperature and melting point are measured by conventional methods, in particular using differential scanning calorimetry (DSC) using a heating rate of 10° C./min. The experimental protocol is described in detail in the “Examples” section below.
Advantageously, when the semicrystalline thermoplastic polyester has a heat of fusion of greater than 10 J/g, preferably greater than 20 J/g, the measurement of this heat of fusion consisting in subjecting a sample of this polyester to a heat treatment at 170° C. for 16 hours, then in evaluating the heat of fusion by DSC by heating the sample at 10° C./min.
The semicrystalline thermoplastic polyester according to the invention in particular has a lightness L* greater than 40. Advantageously, the lightness L* is greater than 55, preferably greater than 60, most preferentially greater than 65, for example greater than 70. The parameter L* may be determined using a spectrophotometer, via the CIE Lab model.
Finally, the reduced solution viscosity of said semicrystalline thermoplastic polyester is greater than 50 ml/g and preferably less than 120 ml/g, this viscosity being able to be measured using an Ubbelohde capillary viscometer at 25° C. in an equi-mass mixture of phenol and ortho-dichlorobenzene after dissolving the polymer at 130° C. with stirring, the concentration of polymer introduced being 5 g/I.
This test for measuring reduced solution viscosity is, due to the choice of solvents and the concentration of the polymers used, perfectly suited to determining the viscosity of the viscous polymer prepared according to the process described below.
The semicrystalline nature of the thermoplastic polyesters used according to the present invention is characterized when the latter, after a heat treatment of 16 h at 170° C., have X-ray diffraction lines or an endothermic melting peak in differential scanning calorimetry (DSC) analysis.
The semicrystalline thermoplastic polyester as defined above has many advantages for the production of fibers.
Indeed, by virtue in particular of the molar ratio of 1,4:3,6-dianhydrohexitol units (A)/sum of 1,4:3,6-dianhydrohexitol units (A) and alicyclic diol units (B) other than 1,4:3,6-dianhydrohexitol units (A) of at least 0.05 and at most 0.30 and of a reduced solution viscosity of greater than 50 ml/g and preferably less than 120 ml/g, the semicrystalline thermoplastic polyesters make it possible to produce fibers which have a better heat resistance and improved mechanical properties compared with for example conventional fibers produced from polyethylene isosorbide terephthalate (PEIT).
The fibers according to the invention may be directly produced from the melt state after polymerization of the semicrystalline thermoplastic polyester.
According to one alternative, the semicrystalline thermoplastic polyester may be packaged in a form that is easy to handle, such as pellets or granules, before being used for the production of fibers. Preferentially, the semicrystalline thermoplastic polyester is packaged in the form of granules, said granules being advantageously dried before conversion into the form of fibers. The drying is carried out so as to obtain granules having a residual moisture content of less than 300 ppm, preferentially less than 200 ppm, for instance approximately 180 ppm. The fibers produced may be monofilaments or multifilaments.
The fibers produced from the semicrystalline thermoplastic polyester according to the invention can be obtained by the methods known to those skilled in the art, for example melt spinning, or by (wet or dry) solution processes. Preferentially, the fibers are produced by the melt-spinning method.
The production of fibers by the melt-spinning method consists first in melting the polyester in an extruder. The molten material is then sent under pressure through a die constituted of a multitude of holes. At the die outlet, the filaments are air-cooled, drawn and coil-wound. Generally, a sizing product is applied at the lower part of the spinning chimney.
According to one particular embodiment, the semicrystalline thermoplastic polyester previously defined is used in combination with one or more additional polymers for the production of fibers.
The additional polymer may be chosen from polyamides, polyesters other than the polyester according to the invention, polystyrene, styrene copolymers, styrene-acrylonitrile copolymers, styrene-acrylonitrile-butadiene copolymers, poly(methyl methacrylate)s, acrylic copolymers, poly(ether-imide)s, poly(phenylene oxide)s such as poly(2,6-dimethylphenylene oxide), poly(phenylene sulfate)s, poly(ester-carbonate)s, polycarbonates, polysulfones, polysulfone ethers, polyether ketones, and mixtures of these polymers.
The additional polymer may also be a polymer which makes it possible to improve the impact properties of the polymer, especially functional polyolefins such as functionalized ethylene or propylene polymers and copolymers, core-shell copolymers or block copolymers.
One or more additives may be added during the production of the fiber from the semicrystalline thermoplastic polyester in order to give it particular properties.
Thus, by way of examples of additives, mention may be made of fillers or fibers of organic or mineral, nanometric or non-nanometric, functionalized or non-functionalized nature. They may be silicas, zeolites, glass fibers or beads, clays, mica, titanates, silicates, graphite, calcium carbonate, carbon nanotubes, wood fibers, carbon fibers, polymer fibers, proteins, cellulose-based fibers, lignocellulosic fibers and non-destructured granular starch. These fillers or fibers can make it possible to improve the hardness, the rigidity or the water- or gas-permeability.
The additive may also be chosen from opacifiers, dyes and pigments. They may be chosen from cobalt acetate and the following compounds: HS-325 Sandoplast® Red BB (which is a compound bearing an azo function, also known under the name Solvent Red 195), HS-510 Sandoplast® Blue 2B which is an anthraquinone, Polysynthren® Blue R, and Clariant® RSB Violet.
The additive may also be a UV-resistance agent such as, for example, molecules of benzophenone or benzotriazole type, such as the Tinuvin™ range from BASF: tinuvin 326, tinuvin P or tinuvin 234, for example, or hindered amines such as the Chimassorb™ range from BASF: Chimassorb 2020, Chimasorb 81 or Chimassorb 944, for example.
The additive may also be a fire-proofing agent or flame retardant, such as, for example, halogenated derivatives or non-halogenated flame retardants (for example phosphorus-based derivatives such as Exolit® OP) or such as the range of melamine cyanurates (for example Melapur™: melapur 200), or else aluminum or magnesium hydroxides.
The use according to the present invention of semicrystalline thermoplastic polyester for the production of fibers is particularly advantageous.
This is because the fibers thus produced from semicrystalline thermoplastic polyester as previously described, with in particular a molar ratio of 1,4:3,6-dianhydrohexitol units (A)/sum of 1,4:3,6-dianhydrohexitol units (A) and alicyclic diol units (B) other than 1,4:3,6-dianhydrohexitol units (A) of at least 0.05 and at most 0.30 and a reduced solution viscosity of greater than 50 ml/g, have notable properties, from the point of view of both the mechanical properties and the thermal properties.
Indeed, the fibers produced according to the invention, which may be monofilament or multifilament, exhibit an improvement in the mechanical properties, such as elongation at break or else persistence, and thus have a most particular application for the obtaining of drawn fibers, of nonwoven assemblies, of textiles or geotextiles which are woven or else of cords for various applications, such as tire reinforcements, and also expandable and technical cords and fibers.
A second subject of the invention relates to a process for producing a fiber, said process comprising the following steps of:
The preparation step can be carried out by the methods known to those skilled in the art which are conventionally implemented for the production of fibers.
Thus, by way of example, the preparation step can be carried out by the melt-spinning method or by (wet or dry) solution processes. Preferentially, the preparation step is carried out by the melt-spinning method.
A third subject of the invention relates to a fiber comprising the semicrystalline thermoplastic polyester described above. The fiber according to the invention may also comprise an additional polymer and/or one or more additives as defined above.
The fibers according to the invention may be subjected to one or more additional treatments.
Thus, the fibers may be used for the production of textiles and of nonwovens. The textiles may in particular be obtained by weaving or knitting.
A nonwoven is a manufactured product consisting of a web, a cloth, a lap, a mattress of directionally or randomly distributed fibers, the internal cohesion of which is provided by mechanical, physical or chemical methods or else by a combination of these methods. An example of internal cohesion may be adhesive-bonding, and results in the obtaining of a nonwoven cloth, said nonwoven cloth possibly then being made into the form of a mat of fibers.
The fibers may be converted into a nonwoven according to the techniques known to those skilled in the art, such as the dry route, the melt route, the wet route or flash spinning.
By way of example, the formation of the nonwoven by the dry route may in particular be carried out by calendering or by an airlaid process. With regard to the production by the melt route, it can be carried out by extrusion (spinbonding technology or spunbonded fabric) or by extrusion blow-molding (melt-blown).
The semicrystalline thermoplastic polyester that is particularly suited to the production of fibers may be prepared by a synthesis process comprising:
This first stage of the process is carried out in an inert atmosphere, that is to say under an atmosphere of at least one inert gas. This inert gas may especially be dinitrogen. This first stage may be carried out under a gas stream and it may also be carried out under pressure, for example at a pressure of between 1.05 and 8 bar.
Preferably, the pressure ranges from 3 to 8 bar, most preferentially from 5 to 7.5 bar, for example 6.6 bar. Under these preferred pressure conditions, the reaction of all the monomers with one another is promoted by limiting the loss of monomers during this stage.
Prior to the first stage of oligomerization, a step of deoxygenation of the monomers is preferentially carried out. It can be carried out for example once the monomers have been introduced into the reactor, by creating a vacuum then by introducing an inert gas such as nitrogen thereto. This vacuum-inert gas introduction cycle can be repeated several times, for example from 3 to 5 times. Preferably, this vacuum-nitrogen cycle is carried out at a temperature of between 60 and 80° C. so that the reagents, and especially the diols, are totally molten. This deoxygenation step has the advantage of improving the coloration properties of the polyester obtained at the end of the process.
The second stage of condensation of the oligomers is carried out under vacuum. The pressure may decrease continuously during this second stage by using pressure decrease ramps, in steps, or else using a combination of pressure decrease ramps and steps. Preferably, at the end of this second stage, the pressure is less than 10 mbar, most preferentially less than 1 mbar.
The first stage of the polymerization step preferably has a duration ranging from 20 minutes to 5 hours. Advantageously, the second stage has a duration ranging from 30 minutes to 6 hours, the beginning of this stage consisting of the moment at which the reactor is placed under vacuum, that is to say at a pressure of less than 1 bar.
The process also comprises a step of introducing a catalytic system into the reactor.
This step may take place beforehand or during the polymerization step described above.
Catalytic system is intended to mean a catalyst or a mixture of catalysts, optionally dispersed or fixed on an inert support.
The catalyst is used in amounts suitable for obtaining a high-viscosity polymer in accordance with the use according to the invention for the production of fibers.
An esterification catalyst is advantageously used during the oligomerization stage. This esterification catalyst can be chosen from derivatives of tin, titanium, zirconium, hafnium, zinc, manganese, calcium and strontium, organic catalysts such as para-toluenesulfonic acid (PTSA) or methanesulfonic acid (MSA), or a mixture of these catalysts. By way of examples of such compounds, mention may be made of those given in application US 2011/282020 A1 in paragraphs [0026] to [0029], and on page 5 of application WO 2013/062408 A1.
Preferably, a zinc derivative or a manganese, tin or germanium derivative is used during the first stage of transesterification.
By way of example of amounts by weight, use may be made of from 10 to 500 ppm of metal contained in the catalytic system during the oligomerization stage, relative to the amount of monomers introduced.
At the end of transesterification, the catalyst from the first step can be optionally blocked by adding phosphorous acid or phosphoric acid, or else, as in the case of tin(IV), reduced with phosphites such as triphenyl phosphite or tris(nonylphenyl) phosphites or those cited in paragraph [0034] of application US 2011/282020 A1.
The second stage of condensation of the oligomers may optionally be carried out with the addition of a catalyst. This catalyst is advantageously chosen from tin derivatives, preferentially derivatives of tin, titanium, zirconium, germanium, antimony, bismuth, hafnium, magnesium, cerium, zinc, cobalt, iron, manganese, calcium, strontium, sodium, potassium, aluminum or lithium, or of a mixture of these catalysts. Examples of such compounds may for example be those given in patent EP 1 882 712 B1 in paragraphs [0090] to [0094].
Preferably, the catalyst is a tin, titanium, germanium, aluminum or antimony derivative, and most preferentially tin or germanium.
By way of example of amounts by weight, use may be made of from 10 to 500 ppm of metal contained in the catalytic system during the stage of condensation of the oligomers, relative to the amount of monomers introduced.
Most preferentially, a catalytic system is used during the first stage and the second stage of polymerization. Said system advantageously consists of a catalyst based on tin or of a mixture of catalysts based on tin, titanium, germanium and aluminum.
By way of example, use may be made of an amount by weight of 10 to 500 ppm of metal contained in the catalytic system, relative to the amount of monomers introduced.
According to the preparation process, an antioxidant is advantageously used during the step of polymerization of the monomers. These antioxidants make it possible to reduce the coloration of the polyester obtained. The antioxidants may be primary and/or secondary antioxidants. The primary antioxidant may be a sterically hindered phenol, such as the compounds Hostanox® 0 3, Hostanox® 0 10, Hostanox® 0 16, Ultranox® 210, Ultranox® 276, Dovernox® 10, Dovernox® 76, Dovernox® 3114, Irganox® 1010 or Irganox® 1076 or a phosphonate such as Irgamod® 195. The secondary antioxidant may be trivalent phosphorus compounds such as Ultranox® 626, Doverphos® S-9228, Hostanox® P-EPQ or Irgafos 168.
It is also possible to introduce as polymerization additive into the reactor at least one compound that is capable of limiting unwanted etherification reactions, such as sodium acetate, tetramethylammonium hydroxide or tetraethylammonium hydroxide.
Finally, the process comprises a step of recovering the polyester resulting from the polymerization step. The semicrystalline thermoplastic polyester thus recovered can then be formed as described above.
According to one variant of the synthesis process, a step of increasing the molar mass is carried out after the step of recovering the semicrystalline thermoplastic polyester.
The step of increasing the molar mass is carried out by post-polymerization and may consist of a step of solid-state polycondensation (SSP) of the semicrystalline thermoplastic polyester or of a step of reactive extrusion of the semicrystalline thermoplastic polyester in the presence of at least one chain extender.
Thus, according to a first variant of the production process, the post-polymerization step is carried out by SSP.
SSP is generally carried out at a temperature between the glass transition temperature and the melting point of the polymer. Thus, in order to carry out the SSP, it is necessary for the polymer to be semicrystalline. Preferably the latter has a heat of fusion of greater than 10 J/g, preferably greater than 20 J/g, the measurement of this heat of fusion consisting in subjecting a sample of this polymer of lower reduced solution viscosity to a heat treatment at 170° C. for 16 hours, then in evaluating the heat of fusion by DSC by heating the sample at 10 K/min.
Advantageously, the SSP step is carried out at a temperature ranging from 190 to 280° C., preferably ranging from 200 to 250° C., this step imperatively having to be carried out at a temperature below the melting point of the semicrystalline thermoplastic polyester.
The SSP step may be carried out in an inert atmosphere, for example under nitrogen or under argon or under vacuum.
According to a second variant of the production process, the post-polymerization step is carried out by reactive extrusion of the semicrystalline thermoplastic polyester in the presence of at least one chain extender.
The chain extender is a compound comprising two functions capable of reacting, in reactive extrusion, with alcohol, carboxylic acid and/or carboxylic acid ester functions of the semicrystalline thermoplastic polyester. The chain extender may, for example, be chosen from compounds comprising two isocyanate, isocyanurate, lactam, lactone, carbonate, epoxy, oxazoline and imide functions, it being possible for said functions to be identical or different. The chain extension of the thermoplastic polyester may be carried out in any of the reactors capable of mixing a very viscous medium with stirring that is sufficiently dispersive to ensure a good interface between the molten material and the gaseous headspace of the reactor. A reactor that is particularly suitable for this treatment step is extrusion.
The reactive extrusion may be carried out in an extruder of any type, especially a single-screw extruder, a co-rotating twin-screw extruder or a counter-rotating twin-screw extruder. However, it is preferred to carry out this reactive extrusion using a co-rotating extruder.
The reactive extrusion step may be carried out by:
During the extrusion, the temperature inside the extruder is adjusted so as to be above the melting point of the polymer. The temperature inside the extruder may range from 150 to 320° C.
The semicrystalline thermoplastic polyester obtained after the step of increasing the molar mass is recovered and then formed as previously described.
The invention will be understood more clearly by means of the examples below, which are intended to be purely illustrative and do not in any way limit the scope of the protection.
The properties of the polymers were studied via the following techniques:
The reduced solution viscosity is evaluated using an Ubbelohde capillary viscometer at 25° C. in an equi-mass mixture of phenol and ortho-dichlorobenzene after dissolving the polymer at 130° C. with stirring, the concentration of the polymer introduced being 5 g/I.
The thermal properties of the polyesters were measured by differential scanning calorimetry (DSC): The sample is first heated under a nitrogen atmosphere in an open crucible from 10° C. to 320° C. (10° C.min−1), cooled to 10° C. (10° C.min−1), then heated again to 320° C. under the same conditions as the first step. The glass transition temperatures were taken at the mid-point of the second heating. Any melting points are determined on the endothermic peak (onset) at the first heating.
Similarly, the enthalpy of fusion (area under the curve) is determined at the first heating.
For the illustrative examples presented below, the following reagents were used:
1,4-Cyclohexanedimethanol (99% purity, mixture of cis and trans isomers)
Isosorbide (purity>99.5%) Polysorb® P from Roquette Freres
Terephthalic acid (99+% purity) from Acros
Irganox® 1010 from BASF AG
Dibutyltin oxide (98% purity) from Sigma-Aldrich
Two thermoplastic polyesters P1 and P2 were prepared.
The first thermoplastic polyester P1 is a semicrystalline thermoplastic polyester prepared according to the procedure below, for use according to the invention with in particular a molar ratio of 1,4:3,6-dianhydrohexitol units (A)/sum of 1,4:3,6-dianhydrohexitol units (A) and alicyclic diol units (B) other than 1,4:3,6-dianhydrohexitol units (A) of at least 0.05 and at most 0.30.
Thus, 1432 g (9.9 mol) of 1,4-cyclohexanedimethanol, 484 g (3.3 mol) of isosorbide, 2000 g (12.0 mol) of terephthalic acid, 1.65 g of Irganox 1010 (antioxidant) and 1.39 g of dibutyltin oxide (catalyst) are added to a 7.5 l reactor. To extract the residual oxygen from the isosorbide crystals, 4 vacuum-nitrogen cycles are carried out once the temperature of the reaction medium is between 60 and 80° C.
The reaction mixture is then heated to 275° C. (4° C./min) under 6.6 bar of pressure and with constant stirring (150 rpm) until a degree of esterification of 87% is obtained. The degree of esterification is estimated from the mass of distillate collected. The pressure is then reduced to 0.7 mbar over the course of 90 minutes according to a logarithmic gradient and the temperature is brought to 285° C.
These vacuum and temperature conditions were maintained until an increase in torque of 12.1 Nm relative to the initial torque is obtained.
Finally, a polymer rod is cast via the bottom valve of the reactor, cooled to 15° C. in a heat-regulated water bath and chopped in the form of granules of about 15 mg.
The resin thus obtained has a reduced solution viscosity of 80.1 ml/g−1.
The 1H NMR analysis of the polyester shows that the final polyester contains 17.0 mol % of isosorbide relative to the diols.
With regard to the thermal properties, the polymer has a glass transition temperature of 96° C., a melting point of 253° C. with an enthalpy of fusion of 23.2 J/g.
A solid-state post-condensation step was carried out on 10 kg of these granules for 20 h at 210° C. under a stream of nitrogen (1500 l/h) in order to increase the molar mass. The resin after solid-state condensation has a reduced solution viscosity of 103.4 ml·g−1.
A second thermoplastic polyester P2 was prepared according to the same procedure as the polyester P1.
This second polyester P2 is a polyester which serves as a comparison and thus has an (A)/[(A)+(B)] molar ratio of 0.44. The amounts of the compounds used are given in detail in table 1 below:
The resin thus obtained with the polyester P2 has a reduced solution viscosity of 54.9 ml/g.
The 1H NMR analysis of the polyester shows that the final polyester contains 44 mol % of isosorbide relative to the diols. With regard to the thermal properties, the polymer has a glass transition temperature of 125° C.
After analysis, the polyester P2 is not characterized by the presence of X-ray diffraction lines and also by the presence of an endothermic melting peak in differential scanning calorimetry (DSC) analysis, even after a heat treatment for 16 h at 170° C. The polyester P2 does not therefore have a crystalline nature
The granules of polyester P1 and P2 obtained in the polymerization step A are dried at 140° C. under nitrogen in order to reach a residual moisture content of the granules of less than 300 ppm and in particular 105 ppm.
The granules are then introduced into an extruder with 5 heating zones: 300° C. for the granule introduction zone, 295° C. in zone 2, 290° C. in zone 3, 285° C. in zone 4, 280° C. in zone 5 and 278° C. in the tube, in the material drive pump and in the filter for removing the gels, and the spinning head (in the direction of circulation of the stream of molten material).
According to this example, the spinning head comprises 10 holes at a flow rate adjusted so as to have a flow rate of material per hole of 1.5 g/minute with a capillary diameter of 0.5 mm and a drive speed of 2000 m/minute. The head used makes it possible to form monofilaments and multifilaments.
At the outlet of the spinning head, a current of air at 25° C. cools the various filaments which are assembled at the point of convergence, then wound by means of a winder.
The fibers obtained with the polyesters P1 and P2 have different characteristics.
Specifically, a filament spun under the conditions above from the semicrystalline thermoplastic polyester P1 containing 17% of isosorbide is drawn with a draw ratio of 7 and has an elongation at break of 7+/−2%. Furthermore, the fibers obtained with the polyester P1 exhibit good strength.
Conversely, a filament drawn under the conditions above from the semicrystalline thermoplastic polyester P2 cannot be drawn with a draw ratio greater than 1.05 because of its fragility. The polyester P2 is therefore absolutely not advantageous for use in the production of fibers.
This reinforces all the more since the semicrystalline thermoplastic polyester according to the invention, having in particular a molar ratio of 1,4:3,6-dianhydrohexitol units (A)/sum of 1,4:3,6-dianhydrohexitol units (A) and alicyclic diol units (B) other than 1,4:3,6-dianhydrohexitol (A) units of at least 0.05 and at most 0.30 and being free of ethylene glycol, is particularly suitable for use in the production of fibers, said fibers, by virtue of their mechanical properties, having advantageous applications in industrial fields such as the textile industry.
| Number | Date | Country | Kind |
|---|---|---|---|
| 16 57031 | Jul 2016 | FR | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/FR2017/052020 | 7/21/2017 | WO | 00 |
