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    • 专利摘要:
    The invention relates to a thermoplastic polyester comprising: ▪ at least one diol tetrahydrofuranedimethanol unit (A); At least one furanedicarboxylic acid unit (B); At least one aliphatic diol unit (C). The invention also relates to a polyester manufacturing process comprising said units (A), (B) and (C).
    公开号:FR3020811A1
    申请号:FR1454176
    申请日:2014-05-09
    公开日:2015-11-13
    发明作者:Nicolas Jacquel；Gabriel Degand；Rene Saint-Loup
    申请人:Roquette Freres SA；
    IPC主号:
    专利说明:

    [0001] Field of the Invention The present invention relates to thermoplastic polyesters comprising tetrahydrofuranedimethanol, aliphatic diol and aromatic diacid units. The invention also relates to a method of manufacturing said polyester and the use of this polyester for the manufacture of compositions and articles. BACKGROUND OF THE INVENTION Because of their many advantages, plastics have become essential for the mass production of objects. Indeed, because of their thermoplastic nature, one can manufacture at high rates any kind of objects from these plastics. Some aromatic polyesters are thermoplastic and have thermal properties allowing them to be used directly for the manufacture of materials. They include aliphatic diol and 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 for the manufacture of containers, packaging or textile fibers. "Monomeric units" means, according to the invention, units included in the polyester which can be obtained after polymerization of a monomer. As regards the ethylene glycol and terephthalic acid units included in the PET, they may be obtained by esterification reaction of ethylene glycol and terephthalic acid, or by a transesterification reaction of ethylene glycol and of ester terephthalic acid. In addition, the development of polyesters from short-term renewable resources has become an ecological and economic imperative in the face of depletion and rising prices of fossil fuels such as oil. One of the important concerns today in the field of polyesters is therefore to provide polyesters of natural origin (biosourcés). Thus, groups such as Danone or Coca-Cola are now marketing partially biobased PET drink bottles, this PET being made from bio-sourced ethylene glycol. A disadvantage of this PET is that it is only partially biobased, since terephthalic acid is derived from fossil resources. Although polyesters comprising biobased terephthalic acid have already been described, for example in the application WO 2013/034743 A1, the processes for the synthesis of biobased terephthalic acid or of a biobased terephthalic acid ester remain too expensive for this purpose. day for the fully biobased PET to become commercially successful. Other aromatic polyesters, including monomeric units other than terephthalic acid units, have been manufactured to substitute PET.
    [0002] Of the biosourced polyesters, the aromatic polyesters comprising aliphatic diol and 2,5-furanedicarboxylic acid (FDCA) units, such as polyethylene-furanoate (PEF), are an interesting alternative because these polyesters have mechanical, optical and thermal properties. close to those of PET. However, these FDCA-based polyesters are manufactured at a temperature generally lower than that of PET. This causes difficulties in obtaining PEF of high molar mass. US Patent Application Publication No. 2011/0282020 A1 discloses a process for the manufacture of a polyester comprising 2,5-furanedicarboxylic acid units in which a 2,5-f uranedicarboxylic acid ester is reacted in a first step with a polyol in the presence of a transesterification catalyst comprising Sn (IV) to form a prepolymer; and then, at reduced pressure in a second step, the prepolymer thus formed is polymerized in the presence of a polycondensation catalyst comprising Sn (II) in order to increase the molar mass thereof and form the polyester. This method makes it possible to manufacture polyesters comprising FDCA units, and in particular to make PEF, of higher molar weight while maintaining low coloration, without requiring a purification step after synthesis. The polymer thus has certain improved properties, such as, for example, superior mechanical properties or even higher viscosity, which allows it to be used for the same applications as PET. However, one of the problems of PEF is that it is, like PET, semi-crystalline and has a crystallinity that remains high. It thus has properties of transparency and impact resistance which may therefore be insufficient. Document US 20130095268 discloses polyesters comprising 2,5-furanedicarboxylic acid and cyclohexanedimethanol (CHDM) units, in particular 1,4-cyclohexanedimethanol, which are useful in the manufacture of fibers, films, bottles, coatings or sheets. It is not indicated whether these polyesters are amorphous or semi-crystalline. On the other hand, when the polyester further comprises an aliphatic diol unit such as ethylene glycol, its glass transition temperature is not, or little, modified regardless of the amount of CHDM units in the polymer chain. This document does not teach that this polyester has a higher molecular weight. Moreover, the Applicant has found that some of the polymers described in this document are semi-crystalline. The Applicant has succeeded in producing an at least partially biosourced polyester having quite satisfactory thermal properties so that it can be converted by conventional thermoplastic techniques. This polyester has a low crystallinity or is totally amorphous. It also has a lower glass transition temperature than PEF, which allows it, by its nature little or no crystalline, to be converted at a lower temperature than the FDCA-based polyesters previously described.
    [0003] SUMMARY OF THE INVENTION The subject of the invention is thus a thermoplastic polyester comprising: at least one diol tetrahydrofuranedimethanol unit (A); at least one furanedicarboxylic acid unit (B); at least one aliphatic diol unit (C) other than the diol (A).
    [0004] This polyester has properties that allow it to be easily transformed by thermoplastic processing techniques. The properties of thermal resistance and its mechanical properties allow it to be used for the manufacture of any type of plastic object. Furthermore, this polyester has a higher molecular weight, relative to a polyester made according to the same process and comprising only aliphatic diol units of type (C). This is very surprising insofar as the alcohol functions of the diol tetrahydrofuranedimethanol have a large steric hindrance, generally greater than that of other aliphatic diols, and in particular greater than the steric hindrance of the alcohol functions of a linear aliphatic diol such as ethylene glycol. Brief Description of the Figures Figure 1 shows the glass transition temperature of a polyester comprising ethylene glycol, furanic acid and THFDM or CHDM units, depending on the amount of THFDM or CHDM in the polyester.
    [0005] Figure 2 shows the 1 H NMR spectrum of a poly (ethylene-co-isosorbide-cotetahydrofuranedimethanol furanoate). DETAILED DESCRIPTION OF THE INVENTION This polyester comprises at least one tetrahydrofuranedimethanol unit (A), at least one aromatic unit (B) and at least one aliphatic diol (C) other than diol (A). By "comprises at least one pattern (X)" is meant that the polyester may comprise different types of patterns (X). Thus, the tetrahydrofuranedimethanol unit (A) may be a unit chosen from the 2,5-tetrahydrofuranedimethanol, 2,4-tetrahydrofuranedimethanol, 2,3-tetrahydrofuranedimethanol and 3,4-tetrahydrofuranedimethanol units or a mixture of these units. Preferably, it is a 2,5-tetrahydrofuranedimethanol unit. The 2,5-tetrahydrofuranedimethanol unit is the following unit: The polyester may also comprise a mixture of isomers of the diols mentioned above. For example, with regard to the 2,5-tetrahydrofuranedimethanol unit, it may be, according to its conformation, in the following isomeric forms: ## STR1 ## meso (cis) 2S-5S (trans) 2R-5R (trans) ).
    [0006] Tetrahydrofuran-dimethanol can be obtained by different reaction routes. It is preferably obtained at least in part from bio-based resources. By way of example, tetrahydrofuranedimethanol may be obtained from diformylfuran as described in application PCT / FR2013 / 052272 in the name of the Applicant. The furanedicarboxylic acid unit (B) may be a 2,5-furanedicarboxylic acid unit, a 2,4-furanedicarboxylic acid unit, a 2,3-furanedicarboxylic acid unit, a 3,4-furanedicarboxylic acid unit or a mixture of these reasons. Preferably, the furanedicarboxylic acid unit is the 2,5-furanedicarboxylic acid unit.
    [0007] More specifically, "2,5-furanedicarboxylic acid unit" denotes in the present application a pattern of formula: dashed lines designating the bonds through which the pattern is connected to the rest of the polyester, and this regardless of the monomer used to form said pattern. Furanedicarboxylic acid can be bio-sourced. One route for obtaining furanedicarboxylic acid is the oxidation of disubstituted furans, for example 5-hydroxymethylfurofuran. The polyester according to the invention comprises at least one unit (C) chosen from aliphatic diols other than diol (A). Whatever the variant, the polyester according to the invention may in particular comprise, with respect to the total amount of diol units (A) and (C): from 1 to 99 units (A), advantageously from 5 to 98; and from 1 to 99 units (C), advantageously from 2 to 95. The aliphatic diol unit may be at least one unit selected from linear aliphatic diols (C1), cycloaliphatic diols (C2), branched aliphatic diols ( C3), or a mixture of these motifs. According to a first advantageous embodiment, the aliphatic diol unit (C) is a linear aliphatic diol unit (C1) or a mixture of these units. The linear aliphatic diol unit (C1) has the following form: wherein the group R is a linear aliphatic group, the dotted lines denoting the bonds through which the unit is connected to the remainder of the polyester, and this that is the monomer used to form said pattern. Preferably, the group R is a saturated aliphatic group. The diol (C1) is preferably chosen from ethylene glycol, 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,8-octanediol, 1,10-decanediol, or a mixture of aliphatic diol units comprising at least one of these units, preferably ethylene glycol and 1,4-butanediol, very preferably ethylene glycol. According to this first embodiment, the polyester according to the invention advantageously comprises, with respect to the total amount of diol units (A) and (C1): from 1 to 99 units (A), advantageously from 5 to 90, preferably from 10 to at 80, for example from 20 to 75; and from 1 to 99 units (C1), advantageously from 10 to 95, preferably from 20 to 90, for example from 25 to 80. According to a second advantageous embodiment, the aliphatic diol unit (C) is at least one unit cycloaliphatic diol (C2) or a mixture of these motifs.
    [0008] According to this second embodiment, the polyester according to the invention advantageously comprises, with respect to the total amount of diol units (A) and (C2): from 1 to 99 units (A), advantageously from 5 to 98, preferably from 80 to at 95; and from 1 to 99 units (C2), advantageously from 2 to 95, preferentially from 5 to 20. According to a first sub-variant, the unit (C2) is chosen from the following units: and or a mixture of these units. Advantageously, (C2) is a 1: 4, 3: 6 dianhydrohexitol unit chosen from: isosorbide; isomannide; isoidide; or a mixture of these patterns. It is preferentially a unit: isosorbide, isomannide and isoidide can thus be obtained respectively by dehydration of sorbitol, mannitol and iditol. The synthesis of these dianhydrohexitols is well known: various routes are described for example in the articles of Fletcher et al. (1,4,3,6-Hexitol dianhydride, I-isoidide, J Am Chem Soc, 1945, 67: 1042-3 and 1,4,3,6-Dianhydro-1-iditol and the structure of isomannide and isosorbide JA Chem Soc, 1946, 68: 939-41), Montgomery et al. (Anhydrides of Polyhydric Alcohols, IV Constitution of Dianhydrosorbitol, J Chem Soc, 1946, 390-3 & Anhydrides of Polyhydric Alcohols, IX Derivatives of 1,4-anhydrosorbitol from 1,4,3,6-dianhydrosorbitol, J Chem Soc 1948, 237-41), de Fleche et al. (Isosorbide, Preparation, Properties and Chemistry, Starch / Staerke 1986, 38: 26-30), Fukuoka et al. (Catalytic conversion of cellulose into sugar Alcohols, Angew Chem Int Ed, 2006, 45: 5161-3), in US Patent 3,023,223. The unit (C2) may also be a cyclobutanediol unit, for example tetramethylcyclobutanediol, in particular a unit chosen from: or a mixture of these units. The unit (C2) may also be a cyclohexanedimethanol unit, in particular a unit chosen from 1,4-cyclohexanedimethanol, 1,2-cyclohexanedimethanol and 1,3-cyclohexanedimethanol units or a mixture of these diols and isomers of these diols. These diols can be in cis or trans configuration. For example, in the case of a 1,4cyclohexanedimethanol unit, they are: for the cis configuration; fço for the trans configuration. The unit (C2) may also be chosen from: 2,3: 4,5-di-O -methylene-galactitol 2,4: 3,5-di-O -methylene-D-mannitol; 2,4: 3,5-di-O-methylene-D-glucitol; or a mixture of these patterns. 2,3: 4,5-di-O-methylene-galactitol can be obtained by acetalization and reduction of galactaric acid, as described by Lavilla et al. in Bio-based poly (butylene terephthalate) copolyesters containing bicyclic diacetalized galactitol and galactaric acid: Influence of composition on properties, Polymer, 2012, 53 (16), 3432-3445. 2,4: 3,5-di-O-methylene-D-mannitol can be obtained by acetalizing D-mannitol with formaldehyde, as described by Lavilla et al. In accordance with the invention, the polyester may comprise mixtures of units (C2) as described in the two subclasses of the present invention. -Variantes previous. According to a third advantageous embodiment, the aliphatic diol unit (C) is a mixture of at least one linear aliphatic diol (C1) and at least one cycloaliphatic diol unit (C2). The diols (C1) and (C2) can be chosen from those listed above. The polyester according to the invention advantageously comprises, with respect to the total amount of diol units (A) and (C): from 1 to 98 units (A), advantageously from 5 to 95, preferentially from 15 to 90; from 1 to 98 units (C1), advantageously from 2 to 60, preferentially from 4 to 50; and from 1 to 98 units (C2), advantageously from 2 to 60, preferably from 5 to 40. In the case where the polyester comprises (C3) units, the branched aliphatic diol unit has the following form: in which the group R 'is a branched aliphatic group, the dotted lines denoting the bonds through which the unit is connected to the remainder of the polyester, and this whatever the monomer used to form said pattern. Preferably, the group R 'is a saturated group.
    [0009] The polyester according to the invention may comprise additional monomeric units other than the units (A), (B) and (C). Preferably, the amount of additional monomeric units is, relative to the total sum of the units of the polyester, less than 30%, most preferably less than 10%. The polyester according to the invention may be free of additional monomeric unit. The additional monomeric units may especially be diether units such as diethylene glycol units. These diether units can come from by-products of the polymerization process, that is to say that they can come for example from an etherification reaction between two glycols. To limit this etherification reaction, it is possible to add to the reactor a base limiting this phenomenon, said base may be sodium acetate, sodium hydroxide, tetramethylammonium hydroxide, tetraethylammonium hydroxide or a mixture of these bases. Preferably, the amount of diether units is, relative to the total sum of the polyester units, less than 10%. The polyester according to the invention may be free of diether units. The additional monomeric units may also be additional diacid units other than the aromatic units (B). By way of example, these units may be saturated aliphatic diacid units. As the saturated cyclic aliphatic diacid unit, mention may be made of the 1,4-cyclohexanedioic acid unit. Advantageously, the aliphatic diacid unit is a linear saturated aliphatic diacid unit. These units may be chosen from succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid or a mixture of these diacids. Preferably, the aliphatic diacid is selected from succinic acid and adipic acid, most preferably succinic acid. Preferably, the amount of additional diacid units is, relative to the total sum of the polyester units, less than 30%, most preferably less than 10%. The polyester according to the invention may be free of additional diacid unit. The additional monomeric units may also be hydroxy acid units. By way of example, the hydroxy acid units may be glycolic acid, lactic acid, hydroxybutyric acid, hydroxycaproic acid, hydroxyvaleric acid, 7-hydroxyheptanoic acid, 8-hydroxyoctanoic acid, 9-hydroxynonanoic acid, hydroxymethylfurancarboxylic acid, hydroxybenzoic acid or a mixture of these hydroxy acids. As regards these hydroxy acid units, they are likely to be obtained from a hydroxy acid or a dilactone such as glycolide or lactide. Preferably, the amount of hydroxy acid units is, based on the total sum of polyester units less than 10%. The polyester according to the invention may be free of a hydroxy acid unit. The polyester according to the invention may also comprise chain-extending units.
    [0010] The expression "chain extender" is understood to mean a motif capable of being obtained by a monomer comprising two functions other than the hydroxyl, carboxylic acid and carboxylic acid ester functions, and capable of reacting with these same functions. The functions may be isocyanate, isocyanurate, caprolactam, caprolactone, carbonate, epoxy, oxazoline and imide functions, said functions being identical or different. As chain extenders which may be used in the present invention, mention may be made of: diisocyanates, preferably methylenediphenyl diisocyanate (MDI), isophorone diisocyanate (IPDI), dicyclohexylmethane diisocyanate (H12MDI), toluene diisocyanate (TDI), naphthalene diisocyanate (NDI), hexamethylene diisocyanate (HMDI) or lysine diisocyanate (LDI), the aliphatic diisocyanate of molar mass 600 g / mol obtained from diacid fatty dimers ( DD101410 Diisocyanate), - dimers, trimers and tetramers of diisocyanates, - so-called "isocyanate-free" prepolymers resulting from a reaction of a diol or an amine on a diisocyanate under conditions such that the prepolymer contains a function isocyanate at each of its ends (α,--functional or telechelic polymer) without free diisocyanate being detectable, - dialkylcarbonates, especially dianhydrohexitol dialkylcarbonates, and especially isosorbide dialkylcarbonates, - dicarbamoylcaprolactams, preferably 1,1'-carbonyl-bis-caprolactam, dicarbamoylcaprolactones, diepoxides, compounds having an epoxide function and a halide function, preferably epichlorohydrin, the heterocyclic compounds, preferably the bis-oxazolines, the bis-oxazolin-5-ones and the bis-azalactones, the methylenic or ethylenic diester derivatives, preferably the methyl or ethyl carbonate derivatives, the any mixtures of any two or more of the aforesaid goods. Preferably, the amount of chain extender units is, based on the total sum of the polyester units, less than 10%. The polyester according to the invention may be free of chain extender pattern. The monomeric units may also be polyfunctional units. By "polyfunctional unit" is meant a unit obtainable by reaction of a comonomer capable of reacting with the hydroxide and / or carboxylic acid and / or carboxylic acid ester functions and having a functionality greater than 2. The functions reactive agents of these branching agents can be hydroxide, carboxylic acid, anhydride, isocyanate, isocyanurate, caprolactam, caprolactone, carbonate, epoxy, oxazoline and imide functions, said functions possibly being identical or different, preferably carboxylic acid, hydroxide, epoxide or isocyanate, most preferably carboxylic acid or hydroxide. The functionality of these branching agents can be from 3 to 6, preferably from 3 to 4. Among the branching agents conventionally used, mention may be made of: malic acid, citric or isocitric acid, tartaric acid, trimesic acid, tricarballylic acid, cyclopentane tetracarboxylic acid, trimellitic anhydride, pyromellitic mono or dianhydride, glycerol, pentaerythritol, dipentaerythritol, monoanhydrosorbitol, monoanhydromannitol, epoxidized oils, dihydroxystearic acid, trimethylolpropane, ethers of these polyols, for example glycerol propoxylate (marketed under the name Voranol 450 by Dow Chemical), polymers having lateral epoxide functional groups, triisocyanates, tetraisocyanates and the respective homopolymers of di-, existing tri- and tetraisocyanates, polyanhydrides, alkoxysilanes, preferably tetraethoxysilane. Preferably, the amount of polyfunctional units is, based on the total sum of the polyester units, less than 10%. The polyester according to the invention may be free of a polyfunctional unit. According to another embodiment of the invention, the polyester according to the invention comprises, with respect to the total amount of units: from 5 to 55% of units (A); - from 40 to 60% of reasons (B); from 1 to 50% of units (C); from 0 to 10% of diether units; from 0 to 30% of additional diacid units other than (B), preferentially from 0 to 10%; from 0 to 10% of hydroxyacid units; from 0 to 10% of chain extender units; from 0 to 10% of polyfunctional units. The polyester according to the invention can be partially biobased or even completely biobased. In other words, it is obtained, in part or in whole, from at least partially biosourced monomers.
    [0011] The polyester may be a random copolymer or a block copolymer.
    [0012] Preferably, the polyester according to the invention has a molar ratio of (B) / ((A) + (C) units ranging from 60/40 to 40/60, advantageously from 55/45 to 45/55. Different patterns in the polyester can be determined by 1 H NMR The skilled person can easily find the analytical conditions for determining the amounts of each polyester unit, Figure 2 shows the NMR spectrum of the poly (ethylene-co) isosorbide-co-tetrahydrofuranedimethanol furanoate) The chemical shifts relative to ethylene glycol are between 4.4 and 5.0 ppm, the chemical shifts relative to the furan cycle are between 7.2 and 7.5 ppm, the tetrahydrofuranedimethanol chemical shifts ranged from 3.6 to 5.0 ppm and 1.8 to 2.4 ppm and chemical shifts to isosorbide were around 4.2 ppm, 4.8 ppm, 5.2 ppm and 5.6 ppm The integration of each signal allows to determine the quantity in each Preferably, the polyester according to the invention has a weight average molecular weight greater than 7500 g / mol, preferably greater than 10000 g / mol, most preferably greater than 20000 g / mol. The molar mass of the polyester can be determined by conventional methods, for example by steric exclusion chromatography (SEC) in a mixture of chloroform and 1,1,1,3,3,3-Hexafluoro-2-propanol. in a 98/2 volume ratio. The signal detection can then be performed by a differential refractometer calibrated with methyl polymethacrylate standards. Advantageously, the glass transition temperature of the polymer according to the invention is greater than or equal to 50 ° C, preferably greater than or equal to 55 ° C, or even greater than or equal to 60 ° C. This allows the use of said polymer to form many types of objects having sufficient thermal resistance to be used in many applications. The glass transition temperature of the polyester can be measured by conventional methods, especially using differential scanning calorimetry (DSC) using a heating rate of 10 K / min. The experimental protocol is detailed in the examples section below. Advantageously, the polyester according to the invention has a glass transition temperature of less than or equal to 85 ° C, advantageously less than or equal to 80 ° C, preferably less than or equal to 75 ° C. This makes it possible to transform the polymer at a lower temperature than a PEF or even a PEFg. The polyester object of the present invention can be semi-crystalline or amorphous. Advantageously, the polyester has a degree of crystallinity a degree of crystallinity of less than 50%, preferably less than 35%, preferably is amorphous. Preferably, the polyester according to the invention is amorphous. In this case, it has improved impact resistance and optical properties, without requiring the use of specific shock modifiers or clarifying agents.
    [0013] The invention also relates to a process for producing thermoplastic polyester which comprises: a step of introducing into a monomer reactor comprising at least one diol tetrahydrofuranedimethanol (A), at least one furanedicarboxylic acid (B) and / or a diester of this acid and at least one aliphatic diol (C) other than diol (A) and; a step of polymerizing the monomers to form the polyester comprising: a first stage during which the reaction medium is stirred at a temperature ranging from 140 to 210 ° C to form oligomers; A second stage during which the oligomers formed are stirred under vacuum at a temperature of from 200 to 275 ° C to form the polyester; a step of recovering the polyester after the polymerization step. Using this method, it is possible to obtain a polyester having a glass transition temperature sufficient to be used as a plastic material for the manufacture of any type of object. To carry out the process according to the invention, the various monomers mentioned above can be used. As regards the monomers introduced into the reactor, they may be introduced once or several times into the reactor, in the form of a mixture or separately. The diols (A) and (C) useful for the process of the invention have been described above in the corresponding polyester pattern parts. With regard to the diacid units, including the units (B), they can be obtained from the diacid but it is also possible to replace this diacid with monomers differing only in that the carboxylic acid function of the monomer is substituted. by a carboxylic acid ester function. In this case, preferably used as precursor of the unit B, the alkyl diesters of furanedicarboxylic acid, and in particular alkyl diesters of 2,5-furanedicarboxylic acid. Even more preferentially, the methyl or ethyl diesters, most preferably methyl, is 2,5-dimethylfuranoate.
    [0014] As regards the additional monomeric units, they can be obtained from the monomers cited as patterns of the polyester. In the case of units carrying acid functions, they may be obtained by monomers differing only from the monomers mentioned in that the carboxylic acid function of the monomer is substituted with a carboxylic acid ester function or, where these monomers exist, by an anhydride function. Preferably, relative to all the moles of monomers (A), (B) and (C) introduced into the reactor, the molar percentage of acid and / or diester (B) ranges from 25 to 45%. Indeed, in the process according to the invention, it is preferred to use an excess of diol in order to carry out the synthesis of the polyester. This makes it possible to accelerate the reaction and also to increase the final molar mass of the polyester thus formed. Those skilled in the art will be able to adjust the amounts of diol (A) and (C) introduced into the reactor in order to obtain the respective proportions in the various diols of the polyesters according to the invention described above. For example, with respect to all the moles of diol (A) and (C), at least 1 mol% and at most 99 mol% are composed of diol (A), advantageously from 5 to 98%. the temperature during the first polymerization stage ranges from 150 to 200 ° C. Preferably, this first stage is in an inert gas atmosphere, this gas may in particular be dinitrogen. This first stage can be done under gas flow. It can also be done under pressure, for example at a pressure between 1.05 and 8 bar.
    [0015] Preferably, when the monomer (B) is of acidic type, the pressure ranges from 3 to 8 bar. Preferably, when the monomer (B) is of ester type, the pressure is from 1.05 to 3 bar. Prior to the first stage, a deoxygenation step of the reactor is preferably carried out. It can be done for example by carrying out the vacuum in the reactor and then introducing an inert gas such as nitrogen into the reactor. This empty cycle of introduction of inert gas can be repeated several times, for example 3 to 5 times. Preferably, this vacuum-nitrogen cycle is carried out at a temperature between 60 and 80 ° C so that the reactants, and especially the bicyclic diols, are completely melted. This deoxygenation step has the advantage of improving the coloring properties of the polyester obtained at the end of the process.
    [0016] The second stage of polymerization is carried out under vacuum, preferably at a pressure of less than 10 mbar, most preferably less than 1 mbar. Preferably, the temperature during the second polymerization stage ranges from 220 to 270 ° C. According to the invention, the first stage of the polymerization stage preferably has a duration ranging from 1 to 5 hours. Advantageously, the second stage has a duration ranging from 2 to 6 hours. The process according to the invention comprises a polymerization step in the presence of a catalyst. Advantageously, during this stage, a transesterification catalyst is used. This transesterification catalyst may be chosen from tin derivatives, preferably tin (IV), titanium, zirconium, hafnium, zinc, manganese, calcium and strontium derivatives, organic catalysts such as para-toluene sulfonic acid (APIS), methanesulfonic acid (AMS) or a mixture of these catalysts. As examples of such compounds, mention may be made of those given in application US2011282020A1 in paragraphs [0026] to [0029], and on page 5 of application WO 2013/062408 A1. Preferably, during the first stage of transesterification, an IV tin derivative, a titanium derivative, a zinc derivative or a manganese derivative is used. At the end of transesterification, the catalyst of the first step may be optionally blocked by the addition of phosphorous acid or phosphoric acid, or else as in the case of tin (IV) reduced by phosphites such as phosphite triphenyl or phosphite tris (nonylphenyl) or those cited in paragraph [0034] of the application US 2011282020A1. The second polymerization stage (polycondensation) may optionally be carried out with the addition of an additional catalyst. This catalyst is advantageously chosen from tin derivatives, preferably tin (II), titanium, zirconium, germanium, antimony, bismuth, hafnium, magnesium, cerium, zinc, cobalt, iron, manganese, calcium, strontium, sodium, potassium, aluminum, lithium or a mixture of these catalysts. By way of example of such compounds, mention may be made of those given in EP 1882712 B1 in paragraphs [0090] to [0094]. Preferably, the catalyst is a tin (II), titanium, germanium or antimony derivative.
    [0017] Most preferably, a titanium-based catalyst is used during the first stage and the second stage of polymerization. The polyester recovered during the last stage of the process advantageously has the characteristics previously given.
    [0018] The method according to the invention comprises a step of recovering the polyester at the end of the polymerization step. The polyester can be recovered by extracting it from the reactor in the form of a melted polymer rod. This ring can be converted into granules using conventional granulation techniques. The method according to the invention may also comprise, after the step of recovering the polyester, a solid state polymerization step. The subject of the invention is also a polyester that can be obtained according to the process of the invention. The invention also relates to a composition comprising, in addition to the polyester according to the invention, at least one additive or an additional polymer or a mixture thereof.
    [0019] Thus, the composition according to the invention can also comprise, as additive, fillers or fibers of organic or inorganic nature, nanometric or non-functionalized or non-functionalized. It can be silicas, zeolites, fibers or glass beads, clays, mica, titanates, silicates, graphite, calcium carbonate, carbon nanotubes, wood fibers, of carbon fibers, polymer fibers, proteins, cellulosic fibers, lignocellulosic fibers and non-destructured granular starch. These fillers or fibers can improve the hardness, rigidity or permeability to water or gases. The composition may comprise from 0.1 to 75% by weight filler and / or fibers relative to the total weight of the composition, for example from 0.5 to 50%. The composition may also be of composite type, that is to say include large amounts of these fillers and / or fibers. The additive useful for the composition according to the invention may also comprise opacifying agents, dyes and pigments. They can be selected from cobalt acetate and the following compounds: HS-325 Sandoplast® RED BB (which is a compound carrying an azo function also known as Solvent Red 195), HS-510 Sandoplast® Blue 2B which is an anthraquinone, Polysynthren® Blue R, and Clariant® RSB Violet. The composition may also include as an additive a process agent, or processing aid, to reduce the pressure in the processing tool. A release agent to reduce adhesion to polyester forming materials such as molds or calender rolls can also be used. These agents can be selected from esters and fatty acid amides, metal salts, soaps, paraffins or hydrocarbon waxes. Specific examples of these agents are zinc stearate, calcium stearate, aluminum stearate, stearamide, erucamide, behenamide, beeswax or candelilla waxes. The composition according to the invention may also comprise other additives such as stabilizing agents, for example light stabilizing agents, UV stabilizing agents and heat stabilizing agents, fluidifying agents, flame retardants and antistatic agents. It may also include primary and / or secondary antioxidants. The primary antioxidant can be a sterically hindered phenol such as the compounds Hostanox® 0 3, Hostanox® 010, Hostanox® 016, Ultranox® 210, Ultranox®276, Dovernox® 10, Dovernox® 76, Dovernox® 3114 Irganox® 1010, Irganox® 1076. The secondary antioxidant may be trivalent phosphorus compounds such as Ultranox® 626, Doverphos® S-9228, Hostanox® P-EPQ, or Irgafos® 168.
    [0020] The composition may further comprise an additional polymer, different from the polyester according to the invention. This 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, polymethyl methacrylates and acrylic copolymers. poly (ether-imides), polyphenylene oxide such as (2,6-dimethylphenylene) polyoxide, phenylene polysulfate, poly (ester-carbonates), polycarbonates, polysulfones, polysulfone ethers, polyether ketone and mixtures of these polymers. The composition may also comprise, as additional polymer, a polymer making it possible to improve the impact properties of the polymer, in particular functional polyolefins such as functionalized ethylene or propylene polymers and copolymers, core-shell copolymers or block copolymers. The compositions according to the invention may also comprise polymers of natural origin, such as starch, cellulose, chitosans, alginates, proteins such as gluten, pea proteins, casein, collagen, gelatin, lignin, these polymers of natural origin may or may not be physically or chemically modified. The starch can be used in destructured or plasticized form. In the latter case, the plasticizer may be water or a polyol, in particular glycerol, polyglycerol, isosorbide, sorbitans, sorbitol, mannitol or else urea. In order to prepare the composition, use may especially be made of the process described in document WO 2010/0102822 A1.
    [0021] The composition according to the invention can be manufactured by conventional methods for transforming thermoplastics. These conventional methods include at least one step of melt blending or softening of the polymers and a step of recovering the composition. This method can be carried out in internal mixers with blades or rotors, external mixers, co-rotating or counter-rotating twin screw extruders. However, it is preferred to carry out this mixture by extrusion, in particular by using a co-rotating extruder. The mixture of the constituents of the composition can be carried out under an inert atmosphere. In the case of an extruder, the various constituents of the composition can be introduced by means of introducing hoppers located along the extruder. The invention also relates to an article comprising the polyester or the composition according to the invention. This article can be of any type and be obtained using conventional transformation techniques.
    [0022] It may be, for example, fibers or yarns useful for the textile industry or other industries. These fibers or yarns can be woven to form fabrics or nonwovens. The article according to the invention can also be a film, a sheet. These films or sheets can be manufactured by calendering techniques, cast film extrusion, extrusion blow molding.
    [0023] The article according to the invention may also be a container for transporting gases, liquids and / or solids. It may be bottles, gourds, bottles, for example bottles of sparkling water or not, bottles of juice, bottles of soda, bottles, bottles of alcoholic beverages, vials, for example bottles of medicine, bottles of cosmetic products, dishes, for example for ready meals, microwave dishes or lids. These containers can be of any size. They can be manufactured by extrusion blow molding, thermoforming or injection blow molding. These articles can also be optical articles, that is to say articles requiring good optical properties such as lenses, disks, transparent or translucent panels, optical fibers, films for LCD screens or even windows. These optical articles have the advantage of being able to be placed near sources of light and therefore of heat, while maintaining excellent dimensional stability and good resistance to light.
    [0024] The articles may also be multilayer articles, at least one layer of which comprises the polymer or the composition according to the invention. These articles can be manufactured by a process comprising a coextrusion step in the case where the materials of the different layers are brought into contact in the molten state. By way of example, mention may be made of tube coextrusion techniques, coextrusion of profiles, coextrusion blow molding (in English "blowmolding") of bottles, flasks or tanks, generally grouped under the term coextrusion blow molding of hollow bodies, coextrusion inflation also called blowing of sheath (in English "film blowing") and co-extrusion flat ("in English" cast coextrusion ").
    [0025] They can also be manufactured by a process comprising a step of applying a polyester layer in the molten state to a layer based on organic polymer, metal or adhesive composition in the solid state. This step may be carried out by pressing, overmolding, lamination or lamination, extrusion-rolling, coating, extrusion-coating or coating.
    [0026] The invention will now be illustrated in the examples below. It is specified that these examples do not limit the present invention. Examples Reagents For the illustrative examples presented below the following reagents were used: Monomer A: 2,5-tetrahydrofuranedimethanol (THFDM) (purity 99.6%). Obtained by hydrogenation of 2,5-furanedimethanol (95%, Pennakem) on Ni from Raney at 110 ° C and 70 bar, then purification by distillation. Monomer B: precursor of the "B" motif: 2,5-dimethylfuranoate (purity> 99%) of Satachem Monomer (C): Ethylene glycol (purity> 99.8%) of Sigma-Aldrich Isosorbide (purity> 99.5% ) Polysorb® P from Roquette 2,2,4,4-tetramethyl-1,3-cyclobutanediol (purity> 98%) of Chemical Point, cis / trans ratio = 50/50 1,4-cyclohexanedimethanol cis / trans ratio: 30/70 (purity> 99%) of Sigma Aldrich Catalysts: Titanium isopropoxide (> 99.99%) Sigma Aldrich Titanium tetrabutoxide (> 97%) Sigma Aldrich Analytical techniques NMR 1H NMR analysis of the polyester samples was performed using a Brucker 400MHz spectrometer equipped with a QNP probe. Prior to the analysis, 15 mg of the polyester sample was dissolved in 0.6 ml of deuterated chloroform (CDCl3) and 0.1 ml of tetrafluoroacetic acid (d / TFA). The integration of the peaks corresponding to the various units allowed in particular the calculation of the ratios A / C and A / C1 / C2 given in Tables 1 and 2. Size Exclusion Chromatography The molecular weight of the polymer was evaluated by chromatography. Steric exclusion (SEC) in a mixture of chloroform and 1,1,1,3,3,3-hexafluoro-2-propanol (98: 2 vol%). The polyester samples were dissolved at a concentration of 1 grl and then eluted at a flow rate of 0.75 ml.min-1. Signal acquisition was performed using a refractometric detector (Agilent-RI-1100a) and weight average molecular weights (Mw) were subsequently evaluated using polymethyl methacrylate (PMMA) standards. ). DSC The thermal properties of the polyesters were measured by differential scanning calorimetry (DSC): The sample is first heated from 10 to 280 ° C (10 ° C min-1), cooled to 10 ° C (10 ° C) ° C.min-1) and then heated to 280 ° C under the same conditions as the first step. The glass transition was taken at the midpoint of the second heater.
    [0027] Preparation and characterization of thermoplastic polyesters In the following protocols, the proportions of reactants are given in mass proportions. Example according to the invention (Ex. 1): In a reactor are introduced 50 parts of dimethylfuranoate, 28.65 parts of ethylene glycol, 10.92 parts of tetrahydrofuranedimethanol and 4.2 parts of a solution of titanium isopropoxide in toluene (1% by weight of titanium isopropoxide). The mixture is stirred by mechanical stirring at 150 rpm and is placed in an oven heated to 180 ° C in 15 min under nitrogen flow. Always under nitrogen flow, the oven is then maintained at 180 ° C for 1h before being heated again to 210 ° C in 1h. This temperature is maintained for 2 hours in order to eliminate the maximum amount of methanol.
    [0028] Following this, the temperature of the oven is raised to 260 ° C, the pressure is reduced in 90min to 0.7mbar and the stirring speed is reduced to 50 rpm. These conditions are maintained for 3 hours. The characteristics of the polymer formed are reported in Table 1 below. Example according to the invention (Ex. 2) In a reactor are introduced 50 parts of dimethylfuranoate, 30 parts of ethylene glycol, 11 parts of tetrahydrofuranedimethanol and 4.5 parts of a solution of titanium isopropoxide in toluene (1). % by weight of titanium isopropoxide). The mixture is stirred by magnetic stirring bar and is heated to 160 ° C in 30 min under a stream of nitrogen. Still under a stream of nitrogen, the mixture is then maintained at 160 ° C. for 1 hour before being heated again to 190 ° C. over 30 minutes. This temperature is maintained for 2 hours in order to eliminate the maximum amount of methanol. Following this, the temperature of the reactor is raised to 240 ° C, the pressure is reduced in 90min to 0.7mbar with magnetic stirring. These conditions are maintained for 3 hours. The characteristics of the polymer formed are reported in Table 1 below.
    [0029] Example according to the invention (Ex. 3): In a reactor are introduced 50 parts of dimethylfuranoate, 23 parts of ethylene glycol, 23.3 parts of tetrahydrofuranedimethanol and 4.3 parts of a solution of titanium isopropoxide in the reactor. toluene (1% by weight of titanium isopropoxide). The stir bar stirred mixture is heated to 160 ° C over 30 minutes under nitrogen flow. Still under a stream of nitrogen, the mixture is then maintained at 160 ° C. for 1 hour before being heated again to 190 ° C. over 30 minutes. This temperature is maintained for 2 hours in order to eliminate the maximum amount of methanol. Following this, the temperature of the reactor is raised to 240 ° C, the pressure is reduced in 90min to 0.7mbar with magnetic stirring. These conditions are maintained for 3 hours.
    [0030] The characteristics of the polymer formed are reported in Table 1 below.
    [0031] Example according to the invention (Ex. 4) In a reactor are introduced 50.1 parts of dimethylfuranoate, 20 parts of ethylene glycol, 28.7 parts of tetrahydrofuranedimethanol and 4.4 parts of a solution of titanium isopropoxide in toluene (1% by weight of titanium isopropoxide). The stir bar stirred mixture is heated to 160 ° C over 30 minutes under nitrogen flow. Still under a stream of nitrogen, the mixture is then maintained at 160 ° C. for 1 hour before being heated again to 190 ° C. over 30 minutes. This temperature is maintained for 2 hours in order to eliminate the maximum amount of methanol. Following this, the temperature of the reactor is raised to 240 ° C, the pressure is reduced in 90min to 0.7mbar with magnetic stirring. These conditions are maintained for 3 hours. The characteristics of the polymer formed are reported in Table 1 below. Example according to the invention (Ex. 5) 49.8 parts of dimethylfuranoate, 13.2 parts of ethylene glycol, 44 parts of tetrahydrofuranetimethanol and 4.8 parts of a solution of titanium isopropoxide are introduced into a reactor. toluene (1% by weight of titanium isopropoxide). The stir bar stirred mixture was heated at 160 ° C in 30 minutes under nitrogen flow. Still under nitrogen flow, the mixture is then maintained at 160 ° C. for 1 h before being heated again to 190 ° C. in 30 min. This temperature is maintained for 2 hours in order to eliminate the maximum amount of methanol.
    [0032] Subsequently, the temperature of the reactor is raised to 240 ° C., the pressure is reduced in 90 min to 0.7 mbar with magnetic stirring. These conditions will be maintained for 3 hours. The characteristics of the polymer formed are reported in Table 1 below. Comparative Example (CP1) 49.9 parts of dimethylfuranoate, 33.7 parts of ethylene glycol and 4.6 parts of a titanium isopropoxide solution in toluene (1% by weight of toluene) are introduced into a reactor. titanium isopropoxide). The stir bar stirred mixture was heated at 160 ° C in 30 minutes under nitrogen flow. Still under nitrogen flow, the mixture is then maintained at 160 ° C. for 1 h before being heated again to 190 ° C. in 30 min. This temperature is maintained for 2 hours in order to eliminate the maximum amount of methanol.
    [0033] Subsequently, the temperature of the reactor is raised to 240 ° C., the pressure is reduced in 90 min to 0.7 mbar with magnetic stirring. These conditions are maintained for 3 hours.
    [0034] The characteristics of the polymer formed are reported in Table 1 below. Comparative Example (CP2) In a reactor are introduced 50 parts of dimethylfuranoate, 23.6 parts of ethylene glycol, 23.6 parts of cyclohexanedimethanol and 8.42 parts of a solution of titanium tetrabutoxide in toluene (1% by weight). titanium tetrabutoxide mass). The mixture is stirred by mechanical stirring at 150 rpm and is placed in an oven heated to 160 ° C in 15 min under nitrogen flow. Still under a stream of nitrogen, the oven is then maintained at 160 ° C for 1 hour before being heated again to 190 ° C in 1 hour. This temperature is maintained for 2 hours in order to eliminate the maximum amount of methanol. Following this, the temperature of the oven is raised to 260 ° C, the pressure is reduced in 90 min to 0.7 mbar and the stirring speed is reduced to 50 rpm. These conditions are maintained for 3 hours. The characteristics of the polymer formed are reported in Table 1 below. TABLE 1 Properties of the Polyesters According to the Invention and Comparative: Effect of Tetrahydrofuran on poly (ethylene-co-tetrahydrofuranedimethanol furanoate) Polyesters Ex. Tf (° C) (or Tc (° C) (or Tg (° Amorphous C) A or CHDM / C Mw (g / mol) amorphous) (mol / mol) 1 Amorphous Amorphous 78 24.5 / 75.5 22350 2 Amorphous Amorphous 64.8 32.5 / 67.5 44000 3 Amorphous Amorphous 64.2 59.3 / 40.7 52150 4 Amorphous Amorphous 65.6 66.9 / 33.1 103850 5 Amorphous Amorphous 58.4 86.1 / 14.9 128250 CP1 218 176 85 0/100 18450 CP2 208 175 76 62.4 (CHDM) / 37.6 83850 The tests show that: - the use of THFDM type diols made it possible to increase the molar mass of the polyester obtained. (cf CP1 vs Ex 1 to 5 or CP 2 vs Ex4) -A comparable amount of cycloaliphatic monomer, the polyester according to the invention has a lower glass transition temperature, which allows it to be converted to lower temperature. This glass transition temperature is lower than that of PET, but the polyester according to the invention remains quite satisfactory for many applications Moreover, unlike all the examples of polyesters according to the invention which are amorphous, some polyesters comprising furanedicarboxylic acid and cyclohexanedimethanol (CHDM) units are semi-crystalline; it is therefore necessary to transform the latter to a temperature exceeding its melting temperature. Example according to the invention (Ex. 6) In a reactor are introduced 49.7 parts of dimethylfuranoate, 12.7 parts of ethylene glycol, 36.8 parts of tetrahydrofuranedimethanol, 9.9 parts of disosorbide and 5.4 parts of a solution of titanium isopropoxide in toluene (1% by weight of titanium isopropoxide). The stir bar stirred mixture was heated at 160 ° C in 30 minutes under nitrogen flow. Still under a stream of nitrogen, the mixture is then maintained at 160 ° C. for 1 hour before being heated again to 190 ° C. over 30 minutes. This temperature is maintained for 2 hours in order to eliminate the maximum amount of methanol.
    [0035] Following this, the temperature of the reactor is raised to 240 ° C, the pressure is reduced in 90min to 0.7mbar with magnetic stirring. These conditions are maintained for 3 hours. The characteristics of the polymer formed are reported in Table 2 below. Example according to the invention (Ex. 7) In a reactor are introduced 50 parts of dimethylfuranoate, 12.8 parts of ethylene glycol, 36.4 parts of tetrahydrofuranedimethanol, 9.5 parts of isosorbide, and 7.1 parts of a solution of titanium isopropoxide in toluene (1% by weight of titanium isopropoxide). The mixture is stirred by mechanical stirring at 150 rpm and placed in an oven heated to 180 ° C in 15 min under nitrogen flow. Always under nitrogen flow, the oven is then maintained at 180 ° C for 1h before being heated again to 210 ° C in 1h. This temperature is maintained for 2 hours in order to eliminate the maximum amount of methanol. Following this, the temperature of the oven is raised to 260 ° C, the pressure is reduced in 90min to 0.7mbar and the stirring speed is reduced to 50 rpm. These conditions are maintained for 3 hours. The characteristics of the polymer formed are reported in Table 2 below.
    [0036] Example according to the invention (Ex. 8) In a reactor are introduced 50.1 parts of dimethylfuranoate, 9.8 parts of ethylene glycol, 43 parts of tetrahydrofuranedimethanol, 13.8 parts disosorbide and 5.2 parts of a solution of titanium isopropoxide in toluene (1% titanium isopropoxide). The stir bar stirred mixture is heated to 160 ° C over 30 minutes under nitrogen flow. Still under a stream of nitrogen, the mixture is then maintained at 160 ° C. for 1 hour before being heated again to 190 ° C. over 30 minutes. This temperature is maintained for 2 hours in order to eliminate the maximum amount of methanol. Following this, the temperature of the reactor is raised to 240 ° C, the pressure is reduced in 90min to 0.7mbar with magnetic stirring. These conditions are maintained for 3 hours. The characteristics of the polymer formed are reported in Table 2 below. Example according to the invention (Ex. 9) In a reactor are introduced 50 parts of dimethylfuranoate, 17.1 parts of ethylene glycol, 7.7 parts of tetrahydrofuranedimethanol, 31.3 parts disosorbide and 5 parts of a solution of titanium isopropoxide in toluene (1% titanium isopropoxide). The stir bar stirred mixture is heated to 160 ° C over 30 minutes under nitrogen flow. Still under a stream of nitrogen, the mixture is then maintained at 160 ° C. for 1 hour before being heated again to 190 ° C. over 30 minutes. This temperature is maintained for 2 hours in order to eliminate the maximum amount of methanol.
    [0037] Following this, the temperature of the reactor is raised to 240 ° C, the pressure is reduced in 90min to 0.7mbar with magnetic stirring. These conditions are maintained for 3 hours. The characteristics of the polymer formed are reported in Table 2 below. Example according to the invention (Ex. 10) In a reactor are introduced 50.2 parts of dimethylfuranoate, 58.5 parts of tetrahydrofuranedimethanol, 16.6 parts disosorbide and 5.6 parts of a solution of titanium isopropoxide in the toluene (1% titanium isopropoxide). The stir bar stirred mixture is heated to 160 ° C over 30 minutes under nitrogen flow. Still under a stream of nitrogen, the mixture is then maintained at 160 ° C. for 1 hour before being heated again to 190 ° C. over 30 minutes. This temperature is maintained for 2 hours in order to eliminate the maximum amount of methanol. Following this, the temperature of the reactor is raised to 240 ° C, the pressure is reduced in 90min to 0.7mbar with magnetic stirring. These conditions are maintained for 3 hours. The characteristics of the polymer formed are reported in Table 2 below.
    [0038] Example according to the invention (Ex. 11) In a reactor are introduced 50.2 parts of dimethylfuranoate, 35.6 parts of tetrahydrofuranedimethanol, 8.9 parts of tetramethylcyclobutanediol, 10.3 parts of ethylene glycol and 5.7 parts of a solution of titanium isopropoxide in toluene (1% titanium isopropoxide). The stir bar stirred mixture is heated to 160 ° C over 30 minutes under nitrogen flow. Still under a stream of nitrogen, the mixture is then maintained at 160 ° C. for 1 hour before being heated again to 190 ° C. over 30 minutes. This temperature is maintained for 2 hours in order to eliminate the maximum amount of methanol. Following this, the temperature of the reactor is raised to 240 ° C, the pressure is reduced in 90min to 0.7mbar with magnetic stirring. These conditions are maintained for 3 hours. The characteristics of the polymer formed are reported in Table 2 below. Example according to the invention (Ex. 12) In a reactor are introduced 49.9 parts of dimethylfuranoate, 44.9 parts of tetrahydrofuranedimethanol, 32.3 parts of tetramethylcyclobutanediol, 6.3 parts of a solution of titanium isopropoxide in toluene (1% titanium isopropoxide). The mixture is stirred by magnetic stirring bar and is heated to 160 ° C in 30 min under a stream of nitrogen. Still under a stream of nitrogen, the mixture is then maintained at 160 ° C. for 1 hour before being heated again to 190 ° C. over 30 minutes. This temperature is maintained for 2 hours in order to eliminate the maximum amount of methanol.
    [0039] Following this, the temperature of the reactor is raised to 240 ° C, the pressure is reduced in 90min to 0.7mbar with magnetic stirring. These conditions are maintained for 3 hours. The characteristics of the polymer formed are reported in Table 2 below. Table 2: Properties of polyesters according to the invention comprising different cyclic aliphatic diol units (C2) Examples Nature aliphatic diol Tg (° C) A / C1 / C2 (mol / mol / mol) Mw (g / mol) cyclic C2 6 isosorbide 61.2 73.2 / 19.7 / 7.1 46700 7 isosorbide 64 72.5 / 18.5 / 9 52500 8 isosorbide 58.1 77.1 / 15 / 7.1 45400 9 isosorbide 83.6 19, 6 / 48.6 / 31.8 20400 10 isosorbide 60 88.1 / 0 / 11.9 142300 11 tetramethylcyclobutanediol 50 88.1 / 5 / 6.9 18750 12 tetramethylcyclobutanediol 54 87.9 / 0 / 12.1 1870025 All the polymers according to the invention are amorphous. In addition, these tests show that it is also possible to modulate the glass transition temperature by adding other monomers in the polyester, and especially other cycloaliphatic diol monomers other than tetrahydrofuranedimethanol.
    权利要求:
    Claims (18)
    [0001]
    REVENDICATIONS1. Thermoplastic polyester comprising: - at least one diol tetrahydrofuranedimethanol unit (A); at least one furanedicarboxylic acid unit (B); at least one aliphatic diol unit (C) other than the diol (A).
    [0002]
    2. Polyester according to the preceding claim, characterized in that it has a degree of crystallinity of less than 50%, preferably less than 35%.
    [0003]
    3. amorphous polyester according to one of the preceding claims characterized in that it is amorphous.
    [0004]
    4. Polyester according to one of the preceding claims, characterized in that it has a weight average molecular weight greater than 7500 g / mol, preferably greater than 10000 g / mol, most preferably greater than 20000 g / mol.
    [0005]
    5. Polyester according to one of the preceding claims, characterized in that the aliphatic diol unit (C) is at least one chosen from linear aliphatic diols (C1), cycloaliphatic diols (C2), branched aliphatic diols (C3 ), or a mixture of these patterns.
    [0006]
    6. Polyester according to claim 5, characterized in that the aliphatic diol unit (C) is a linear aliphatic diol unit (C1) or a mixture of these units (C1).
    [0007]
    7. Polyester according to claim 6, characterized in that it comprises, with respect to the total amount of diol units (A) and (C1): from 1 to 99 units (A), advantageously from 5 to 90, preferably from 10 to 80, for example from 20 to 75; and from 1 to 99 units (C1), advantageously from 10 to 95, preferably from 20 to 90, for example from 25 to 80.
    [0008]
    8. Polyester according to claim 5, characterized in that the aliphatic diol unit (C) is a cycloaliphatic diol unit (C2) or a mixture of these units (C2) .SGA / SBu -EN1454176 20.08.2014 32
    [0009]
    9. Polyester according to claim 8, characterized in that it comprises, with respect to the total amount of diol units (A) and (C2): from 1 to 99 units (A), advantageously from 5 to 98, preferentially from 80 to 95; and from 1 to 99 units (C2), advantageously from 2 to 95, preferentially from 5 to 20.
    [0010]
    10. Polyester according to claim 9, characterized in that the aliphatic diol unit (C) comprises at least one mixture of at least one linear aliphatic diol unit (C1) and at least one cycloaliphatic diol unit (C2). 10
    [0011]
    11. Polyester according to claim 10, characterized in that it comprises, relative to the total amount of diol units (A) and (C): from 1 to 98 units (A), advantageously from 5 to 95, preferably from 15 to 90; from 1 to 98 units (C1), advantageously from 2 to 60, preferentially from 4 to 50; and from 1 to 98 units (C2), advantageously from 2 to 60, preferentially from 5 to 40.
    [0012]
    12. Polyester according to one of claims 5 to 7, 10 or 11, characterized in that it comprises at least one linear aliphatic diol unit (C1) selected from ethylene glycol, 1,3-propanediol, 1,4- butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,8-octanediol, 1,10-decanediol, or a mixture of aliphatic diol units comprising at least one of these units, preferentially ethylene glycol and 1,4-butanediol, most preferably ethylene glycol.
    [0013]
    13. Polyester according to one of claims 5 or 8 to 11, characterized in that the cycloaliphatic diol unit (C2) comprises at least one unit selected from the following units: 25SGA / SBu-FR1454176 On 20.08.2014 33; and
    [0014]
    14. Polyester according to claim 13, characterized in that the cycloaliphatic diol unit (C2) comprises at least one unit selected from the following units: preferably a unit
    [0015]
    15. Polyester according to one of the preceding claims, characterized in that it comprises, with respect to the total amount of diol units (A) and (C): - from 1 to 99 units (A), advantageously from 5 to 98; and from 1 to 99 units (C), advantageously from. 2 to 95.SGA / SBu -EN1454176 On 20.08.2014 34
    [0016]
    16. Polyester according to one of the preceding claims characterized in that the glass transition temperature is greater than or equal to 50 ° C, preferably greater than or equal to 60 ° C.
    [0017]
    17. A method of manufacturing thermoplastic polyester characterized in that it comprises: - a step of introduction into a reactor of monomers comprising at least one diol tetrahydrofuranedimethanol (A), at least one furanedicarboxylic acid (B) and / or a diester of this acid and at least one aliphatic diol (C) other than diol (A) and; a step of polymerizing the monomers to form the polyester comprising: a first stage during which the reaction medium is stirred at a temperature ranging from 140 to 210 ° C to form oligomers; a second stage during which the oligomers formed are stirred under vacuum at a temperature ranging from 200 to 275 ° C. in order to form the polyester; a step of recovering the polyester after the polymerization step.
    [0018]
    18. Method according to the preceding claim characterized in that, relative to all the moles of monomers (A), (B) and (C) introduced into the reactor, the molar percentage of acid and / or diester (B ) acid ranges from 25 to 45%.
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    同族专利:
    公开号 | 公开日
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    法律状态:
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    2015-11-13| PLSC| Publication of the preliminary search report|Effective date: 20151113 |
    2016-05-27| PLFP| Fee payment|Year of fee payment: 3 |
    2017-05-30| PLFP| Fee payment|Year of fee payment: 4 |
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    2020-02-14| ST| Notification of lapse|Effective date: 20200108 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1454176A|FR3020811B1|2014-05-09|2014-05-09|THERMOPLASTIC AROMATIC POLYESTERS COMPRISING TETRAHYDROFURANEDIMETHANOL AND FURANEDICARBOXYLIC ACID PATTERNS|FR1454176A| FR3020811B1|2014-05-09|2014-05-09|THERMOPLASTIC AROMATIC POLYESTERS COMPRISING TETRAHYDROFURANEDIMETHANOL AND FURANEDICARBOXYLIC ACID PATTERNS|
    PCT/FR2015/051187| WO2015170050A1|2014-05-09|2015-05-05|Thermoplastic aromatic polyesters comprising tetrahydrofuran-dimethanol and furandicarboxylic acid motifs|
    EP15726235.3A| EP3143068B1|2014-05-09|2015-05-05|Thermoplastic aromatic polyesters comprising tetrahydrofuran-dimethanol and furandicarboxylic acid motifs|
    US15/309,837| US20170145153A1|2014-05-09|2015-05-05|Thermoplastic aromatic polyesters comprising tetrahydrofuran-dimethanol and furandicarboxylic acid motifs|
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