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    • 专利摘要:
    The invention relates to a composition for thermoplastic material comprising: 0 to 70% by weight, preferably 20 to 60% by weight, short reinforcing fibers, 30 to 100% by weight, preferably 40 to 80% by weight, d a thermoplastic matrix based on at least one semicrystalline polyamide polymer, 0 to 50% of additives and / or other polymers, said semi-crystalline polyamide polymer being: a) a reactive composition comprising or consisting of, at least a precursor reactive polyamide prepolymer of said semi-crystalline polyamide polymer, or alternatively to a), b) a non-reactive composition of at least one polyamide polymer, said composition being that of said thermoplastic matrix defined above, and said polyamide prepolymer reagent of the composition a) and said polyamide polymer of the composition b) comprising or consisting of at least one BACT / XT copolyamide.
    公开号:FR3064271A1
    申请号:FR1752485
    申请日:2017-03-24
    公开日:2018-09-28
    发明作者:Mathieu Capelot
    申请人:Arkema France SA；
    IPC主号:
    专利说明:

    ® FRENCH REPUBLIC
    NATIONAL INSTITUTE OF INDUSTRIAL PROPERTY © Publication number:
    (to be used only for reproduction orders)
    ©) National registration number
    064 271
    52485
    COURBEVOIE © Int Cl 8 : C 08 L 77/06 (2017.01), C 08 K 7/02, C 08 G 69/26, C 08 J 5/04, B 29 C 45/00, 47/00
    A1 PATENT APPLICATION
    ©) Date of filing: 24.03.17.(© Priority: (© Applicant (s): ARKEMA FRANCE Public limited company - FR. @ Inventor (s): CAPELOT MATHIEU. ©) Date of public availability of the request: 28.09.18 Bulletin 18/39. ©) List of documents cited in the preliminary search report: See the end of this booklet (© References to other related national documents: (® Holder (s): ARKEMA FRANCE Public limited company. ©) Extension request (s): (© Agent (s): ARKEMA FRANCE Public limited company.
    FR 3 064 271 - A1 (04) SEMI-CRYSTALLINE POLYAMIDE COMPOSITION OF HIGH GLASS TRANSITION TEMPERATURE AND HIGH MELTING TEMPERATURE FOR THERMOPLASTIC MATERIAL, METHOD FOR THE PRODUCTION THEREOF AND USES THEREOF.
    (© The invention relates to a composition for thermoplastic material comprising:
    to 70% by weight, preferably 20 to 60% by weight, of short reinforcing fibers, to 100% by weight, preferably 40 to 80% by weight, of a thermoplastic matrix based on at least one semi-polyamide polymer crystalline, containing 50% of additives and / or other polymers, said semi-crystalline polyamide polymer being:
    a) a reactive composition comprising or consisting of, at least one reactive polyamide prepolymer precursor of said semi-crystalline polyamide polymer, or as an alternative to a),
    b) a non-reactive composition of at least one polyamide polymer, said composition being that of said thermoplastic matrix defined above, and said reactive polyamide prepolymer of composition a) and said polyamide polymer of composition b) comprising or consisting of at least one BACT / copolyamide
    XT.
    -1 SEMI-CRYSTALLINE POLYAMIDE COMPOSITION OF HIGH GLASS TRANSITION TEMPERATURE AND HIGH MELTING TEMPERATURE FOR THERMOPLASTIC MATERIAL, METHOD FOR MANUFACTURING SAME AND USES THEREOF
    The invention relates to a new composition of semi-crystalline polyamide (sc) with a high glass transition temperature, based on bis (aminomethyl) cyclohexane (BAC), for thermoplastic material.
    It also relates to the method of manufacturing said thermoplastic material as well as the uses of said composition for the manufacture of mechanical or structural parts based on said material for pieces of material as well as the resulting part and for applications in the fields of: automotive, rail, marine, road transport, wind, sports, aeronautics and space, building, panels and leisure, as well as electrical and electronic.
    A big challenge in materials is to find a polyamide resin that meets the following specifications:
    - High Tg to have a wide range of service temperatures;
    - A high Tf to have good temperature resistance but low enough to be processable in particular by injection;
    - A very good ability to crystallize so that it can be removed from the mold quickly and thus be compatible with intensive production cycles, such as those used for example in the automobile industry;
    - High rigidity, including hot, to be able to obtain the highest possible modules of the final material.
    Document CN104211953 describes a polyamide composition comprising from 30 to 99.9% by weight of a polyamide resin comprising from 60 to 95% in moles of 10T, from 5 to 40% in moles of 5'T, 5 'corresponding to 2-methyl-1,5-pentamethylenediamine, from 0 to 70% by weight of a reinforcing filler and from 0.1 to 50% by weight of an additive.
    The polyamide resin has a melting temperature above 260 ° C and high molar proportions of 10T.
    EP 550 314 describes, among its examples, (non-reactive) compositions of copolyamide by seeking melting temperatures above 250 ° C. and limited Tg with most of the examples cited having a Tg that is too low (<80 ° C).
    EP 1 988 113 describes a molding composition based on a 10T / 6T copolyamide with:
    at 95% mol of 10T 5 to 40% of 6T.
    -2In particular, polyamides with high molar proportions of 10T and high melting point above 270 ° C are targeted.
    WO 2011/003973 describes compositions comprising from 50 to 95 mol% of a unit based on a linear aliphatic diamine comprising from 9 to 12 carbon atoms and terephthalic acid and from 5 to 50% of unit uniting the terephthalic acid to a mixture of 2,2,4 and 2,4,4 trimethylhexanediamine.
    WO 2014/064375 describes in particular a MXDT / 10T PA which has an excellent compromise between the various characteristics described above. Unfortunately, the meta-xylenediamine monomer (MXD) used is very subject to side reactions, giving rise in particular to the formation of branches.
    The drawbacks of the state of the art, with the absence of a good compromise between the mechanical performances and the aptitude for implementation (ease of transformation) with a shorter production cycle time are overcome by the solution of the present invention which relates to semi-crystalline PA compositions, having an excellent compromise between high mechanical performance (mechanical strength) in particular when hot and an easy implementation in particular by injection. It is in fact of high rigidity and has a glass transition temperature> 150 ° C, a Tf of between 290 ° C and 340 ° C, as well as an excellent ability to crystallize (Tf-Tc <40 ° C), which makes it a matrix of choice for an implementation in particular by injection or molding, in particular for wind, automobile or aeronautics or for electrical and electronics.
    The choice of a semi-crystalline polyamide polymer, as the matrix of the thermoplastic material of the invention, has the advantage, compared with amorphous polyamides, of significantly improved mechanical performance, in particular when hot, such as resistance to creep or to fatigue. In addition, having a melting point above 200 ° C has the advantage in the automotive industry of being compatible with cataphoresis treatments, which an amorphous PA type structure does not allow. A Tg greater than 150 ° C. is sought to ensure good mechanical properties of the thermoplastic material over the entire temperature range of use, in particular for injection. The crystallinity of said polymer must be as high as possible to optimize the mechanical performance and the crystallization speed and / or the highest possible crystallization temperature, this in order to reduce the molding time before ejection of the molded part with a selective choice of the composition of said semi-crystalline polyamide.
    The object of the present invention is the use of new specific compositions of thermoplastic material, in particular based on semi-crystalline polyamide, having a good compromise between high mechanical performance (mechanical strength) in particular when hot and a easy work. More specifically, the
    -3solution of the invention, in the case of reactive compositions, allows using compositions based on semi-crystalline reactive polyamide prepolymers, both improved processability due to the low initial viscosity of the composition, allowing for example d '' use lower injection pressures, or mold parts with a high level of finesse, but also improved mechanical properties due to the high molecular weights achievable. More particularly, the polyamide polymer matrix while having a high Tg and a Tf as defined, with easy processing of said thermoplastic material, must also have a high crystallization speed, characterized first by a difference between melting temperature and crystallization Tf-Tc not exceeding 40 ° C, preferably not exceeding 30 ° C. Therefore, the object of the invention is to develop a polyamide composition meeting the needs already defined above:
    - High Tg to have a wide range of service temperatures;
    - A Tf of 290 ° C to 340 ° C, to be easily processable, in particular by injection;
    - A very good ability to crystallize so that it can be removed from the mold quickly and thus be compatible with intensive production cycles, such as those used for example in the automobile industry;
    - High rigidity, including hot, to be able to obtain the highest possible modules of the final material.
    The present invention relates to a composition for thermoplastic material comprising:
    to 70% by weight, preferably 20 to 60% by weight, of short reinforcing fibers, to 100% by weight, preferably 40 to 80% by weight, of a thermoplastic matrix based on at least one semi-polyamide polymer crystalline, containing 50% of additives and / or other polymers, said semi-crystalline polyamide polymer being:
    a) a reactive composition comprising or consisting of, at least one reactive polyamide prepolymer precursor of said semi-crystalline polyamide polymer, or as an alternative to a)
    b) a non-reactive composition of at least one polyamide polymer, said composition being that of said thermoplastic matrix defined above,
    -4and said reactive polyamide prepolymer of composition a) and said polyamide polymer of composition b) comprising or consisting of at least one BACT / XT copolyamide in which:
    BACT is a unit with amide motif present at a molar level ranging from more than 70% to 99.1%, preferably from 80 to 99%, more preferably from 90 to 99%, where BAC is chosen from 1.3 -bis (aminomethyl) cyclohexyl (1.3 BAC), 1,4bis (aminomethyl) cyclohexyl (1.4 BAC) and a mixture thereof, and T is terephthalic acid,
    - XT is an amide unit present at a molar level ranging from 0.9 to less than
    30%, preferably from 1 to 20%, more preferably from 1 to 10%, where X is a linear aliphatic diamine in C4 to C18, in particular C9 to C18, preferably in C9, C10, C11 and C12, and where T is terephthalic acid, preferably C10, C11 and C12.
    in the BACT and / or XT units, independently of one another, up to 30% by mole, preferably 20% by mole, in particular up to 10% by mole, relative to the total amount of dicarboxylic acids, terephthalic acid can be replaced by other aromatic, aliphatic or cycloaliphatic dicarboxylic acids comprising 6 to 36 carbon atoms, in particular 6 to 14 carbon atoms, and in BACT and / or XT units, independently from each other, up to 30% by mole, preferably 20% by mole, in particular up to 10% by mole, of the BAC and / or depending on the case of X, relative to the amount total of the diamines, can be replaced by other diamines comprising from 4 to 36 carbon atoms, in particular 6 to 12 carbon atoms, and in the copolyamide, not more than 30 mol%, preferably not more than 20% by mole, preferably not more than 10% by mole, relative to the total amount of the monomers, may be formed by lactams or aminocarboxylic acids, and provided that the sum of the monomers which replace terephthalic acid, BAC and X does not exceed a concentration of 30 mol%, preferably 20 mol%, preferably 10% by mole, relative to the total amount of the monomers used in the copolyamide, and provided that BACT and XT units are always present in said polyamide polymer.
    It is obvious that the partial replacements of monomers defined above are understood to respect the ranges of BACT and XT defined above, that is to say 3064271
    -5 say that when BACT is present for example in proportion of more than 70 to 99.1%, the possible partial replacement of BAC and / or T will lead in any case to a final proportion of more than 70% in BACT and likewise for XT.
    The composition according to the invention may include short reinforcing fibers or short fibrous reinforcements.
    Preferably, the so-called short fibers are between 200 and 400 μm in length. These short reinforcing fibers can be chosen from:
    natural fibers mineral fibers, these having high melting temperatures Tf and greater than the melting temperature Tf of said semi-crystalline polyamide of the invention and greater than the polymerization and / or processing temperature.
    polymeric or polymer fibers having a melting temperature Tf 'or failing Tf', a glass transition temperature Tg ', greater than the polymerization temperature or greater than the melting temperature Tf of said semicrystalline polyamide constituting said matrix of material thermoplastic and higher than the processing temperature.
    or mixtures of the fibers mentioned above.
    As mineral fibers suitable for the invention, mention may be made of carbon fibers, which includes fibers of nanotubes or carbon nanotubes (CNTs), carbon nanofibers or graphenes; silica fibers such as glass fibers, in particular of type E, R or S2; boron fibers; ceramic fibers, in particular silicon carbide fibers, boron carbide fibers, boron carbonitride fibers, silicon nitride fibers, boron nitride fibers, basalt fibers; fibers or filaments based on metals and / or their alloys; the fibers of metal oxides, in particular of alumina (AI2O3); metallized fibers such as metallized glass fibers and metallized carbon fibers or mixtures of the abovementioned fibers.
    More particularly, these fibers can be chosen as follows:
    the mineral fibers can be chosen from: carbon fibers, carbon nanotube fibers, glass fibers, in particular of type E, R or S2, boron fibers, ceramic fibers, in particular silicon carbide fibers, carbide fibers boron, boron carbonitride fibers, silicon nitride fibers, boron nitride fibers, basalt fibers, fibers or filaments based on metals and / or their alloys, fibers based on metal oxides like AI2O3, fibers metallic like
    -6 metallized glass fibers and metallized carbon fibers or mixtures of the aforementioned fibers, and the polymer or polymer fibers, under the aforementioned condition, are chosen from:
    fibers of thermosetting polymers and more particularly chosen from: unsaturated polyesters, epoxy resins, vinyl esters, phenolic resins, polyurethanes, cyanoacrylates and polyimides, such as bis-maleimide resins, aminoplasts resulting from the reaction an amine such as melamine with an aldehyde such as glyoxal or formaldehyde, fibers of thermoplastic polymers and more particularly chosen from: polyamide fibers, in particular polyphthalamide fibers, aramid fibers (such as Kevlar®) and aromatic polyamides such as those corresponding to one of the formulas: PPD.T, MPD.I, PAA and PPA, with PPD and MPD being p- and m-phenylene diamine respectively, PAA being polyarylamides and PPA being the polyphthalamides,
    - polyamide block copolymer fibers such as polyamide / polyether, polyarylether ketone fibers (PAEK) such as polyetherether ketone (PEEK), polyetherketone ketone (PEKK), polyetherketoneetherketone ketone (PEKEKK).
    The preferred short reinforcing fibers are short fibers chosen from: carbon fibers, including metallized, glass fibers, including metallized of type E, R, S2, aramid fibers (such as Kevlar®) or polyamides aromatic, polyarylether ketone fibers (PAEK), such as polyetherether ketone (PEEK), polyetherketone ketone fibers (PEKK), polyetherketoneetherketone ketone fibers (PEKEKK) or mixtures thereof.
    Natural fibers can be chosen from flax, castor, wood, sisal, kenaf, coconut, hemp and jute fibers.
    Preferably, the reinforcing fibers present in the composition according to the invention are chosen from glass fibers, carbon fibers, flax fibers and their mixtures, and more preferably glass fibers and carbon fibers, and even more preferably glass fibers.
    Advantageously, the composition of the invention also comprises at least one additive.
    Concerning the additives, without being limited to these, the composition according to a preferred variant of the invention more particularly comprises, specific additives such as thermal stabilizers, in particular these stabilizers are antioxidants against thermo-oxidation and / or photo-oxidation of the polymer of the thermoplastic matrix and are organic or mineral stabilizers.
    The expression “organic stabilizer” or more generally a “combination of organic stabilizers” designates a primary antioxidant of phenol type, a secondary antioxidant of phosphite type and even possibly other stabilizers such as a HALS, which means Hindered Amine Light Stabilize or stabilize light of the hindered amine type (for example Tinuvin 770 from the company Ciba), an anti-UV (for example Tinuvin 312 from the company Ciba), a phenolic stabilizer or based on phosphorus. Amine-type antioxidants such as Naugard 445 from the company Crompton or polyfunctional stabilizers such as Nylostab S-EED from the company Clariant can also be used.
    The organic stabilizer present can be chosen, without this list being restrictive, from:
    - phenolic antioxidants, for example Irganox 245, Irganox 1010, Irganox 1098 from Ciba, Irganox MD1024 from Ciba, Lowinox 44B25 from Great Lakes, ADK Stab AO-80 from Adeka Palmarole.
    stabilizers based on phosphorus, such as phosphites, for example Irgafos 168 from the company Ciba,
    - a UV absorber, such as Tinuvin 312 from Ciba,
    - a HALS, as previously mentioned,
    an amine type stabilizer, such as Naugard 445 from the company Crompton, or also a hindered amine type such as Tinuvin 770 from the company Ciba,
    - a polyfunctional stabilizer such as Nylostab S-EED from Clariant.
    It is obviously possible to envisage a mixture of two or more of these organic stabilizers.
    The expression “mineral stabilizer” designates a stabilizer based on copper or based on a metal oxide as described in US2008 / 0146717. By way of example of such mineral stabilizers, mention may be made of copper halides and acetates or iron oxides such as FeO, Fe 2 O 3 , Fe 3 O 4 or a mixture of these. possibly other metals such as silver, but these are known to be less effective. These copper-based compounds are typically associated with alkali metal halides, in particular potassium.
    These mineral stabilizers are more particularly used, when the structures must have an improved long-term thermal resistance in hot air, in particular for temperatures greater than or equal to 100-120 ° C., since they tend to prevent cuts in polymer chains. .
    More particularly, by stabilizer based on copper, is meant a compound comprising at least one copper atom, in particular in ionic, ionizable form, for example in the form of complex.
    The copper-based stabilizer can be chosen from cuprous chloride, cupric chloride, cuprous bromide, cupric bromide, cuprous iodide, cupric iodide, cuprous acetate and cupric acetate. Mention may be made of halides, acetates of other metals such as silver in combination with the copper-based stabilizer. These copper-based compounds are typically associated with alkali metal halides. A well known example is the mixture of Cul and Kl, where the Cul: Kl ratio is typically between 1: 5 to 1:15. An example of such a stabilizer is the Polyad P201 from the company Ciba.
    More details on copper-based stabilizers can be found in US Patent 2,705,227. More recently, copper-based stabilizers have appeared, such as complexed copper such as the Bruggolen H3336, H3337, H3373 from the company Brüggemann.
    Advantageously, the copper-based stabilizer is chosen from copper halides, copper acetate, copper halides or copper acetate mixed with at least one alkali metal halide, and mixtures thereof, preferably the mixtures of copper iodide and potassium iodide (Cul / KI).
    The additive can also be an impact modifier, advantageously consisting of a polymer having a flexural modulus of less than 100 MPa measured according to ISO standard 178 and of Tg less than 0 ° C. (measured according to standard 11357-2: 2013 at the level of the inflection point of the DSC thermogram), in particular a polyolefin, coupled or not with a Peba (polyether block amide) having a flexural modulus <200 MPa.
    The polyolefin of the impact modifier can be functionalized or non-functionalized or be a mixture of at least one functionalized and / or at least one non-functionalized.
    The additives can also be fillers which can in particular be any filler known to a person skilled in the art in the field of thermoplastic materials. It can in particular be charges which conduct heat and / or conduct electricity, such as metal powder, powdered carbon black, carbon fibrils, carbon nanotubes (NTC), carbide of silicon, boron carbonitride, boron nitride or silicon. We can refer to this subject to the application WO 2010/130930 of the Applicant.
    Reinforcement fibers, whatever they are, long, short or continuous, are excluded from additives and in particular the term "inorganic filler" excludes long, short or continuous reinforcement fibers.
    The additives can also be halogen-free flame retardants, as described in US 2008/0274355 and in particular a metal salt chosen from a metal salt of
    -9phosphinic acid, a metal salt of diphosphinic acid, a polymer containing at least one metal salt of phosphinic acid, a polymer containing at least one metal salt of diphosphinic acid or red phosphorus, an oxide of antimony, a zinc oxide, an iron oxide, a magnesium oxide or metal borates such as a zinc borate or also melamine pyrophosphates and melamine cyanurates. They can also be halogenated flame retardants such as a brominated or polybrominated polystyrene, a brominated polycarbonate or a brominated phenol.
    Advantageously, the additive is chosen from an antioxidant, a heat stabilizer, a UV absorber, a light stabilizer, an impact modifier, a lubricant, an inorganic filler, a flame retardant, a nucleating agent, in particular a mineral filler such as talc, and a dye.
    The expression “other polymers” designates any thermoplastic polymer and in particular a polyamide polymer, in particular an aliphatic, cycloaliphatic or aromatic polyamide, and which can be microcrystalline or amorphous.
    The expression “non-reactive composition” means that the composition is based on a polyamide polymer whose molecular weight is no longer liable to change significantly, that is to say that its molecular mass in number (Mn) changes less than 50% during its implementation and therefore corresponding to the final polyamide polymer of the thermoplastic matrix.
    These polyamides according to composition b) are non-reactive, either by the low rate of reactive (residual) functions present, in particular with a rate of said functions <120 meq / kg, or by the presence of the same type of terminal functions at the end of chain and therefore not reactive with each other, either by the modification and blocking of said reactive functions with a monofunctional reactive component, for example for the amine functions by modification reaction with a monoacid or a monoisocyanate and for carboxyl functions by reaction with a monoamine.
    Advantageously, the molecular weight in number (Mn) of said final polyamide polymer of the thermoplastic matrix of said material is preferably in a range from 6000 to 40,000 g / mol, preferably from 10,000 to 30,000 g / mol as determined by calculation from the rate of terminal functions determined by potentiometric titration in solution and the functionality of said prepolymers or by NMR. These Mn values can correspond to inherent viscosities greater than or equal to 0.7, as determined according to ISO standard 307: 2007 but by changing the solvent (use of mresol instead of sulfuric acid and the temperature being 20 ° C).
    Conversely, the expression “reactive composition” means that the molecular weight of said reactive composition will change during the implementation by reaction of
    - 10 prepolymers reactive with each other by condensation or with a chain extender by polyaddition and without elimination of volatile by-products to lead to the final polyamide polymer of the thermoplastic matrix.
    1,3-BAC (or 1,3 bis (aminomethyl) cyclohexane, CAS No: 2579-20-6) is a cycloaliphatic diamine monomer obtained in particular by hydrogenation of metaxylene diamine (MXDA). 1,3-BAC exists in the form of two isomers, cis and trans, CAS No. 2579-20-6 corresponding to a mixture of isomers.
    1,4-BAC (or 1,4 bis (aminomethyl) cyclohexane, CAS No: 2549-07-9) is a cycloaliphatic diamine monomer obtained in particular by hydrogenation of paraxylene diamine (PXDA). 1,4-BAC exists in the form of two isomers, cis and trans, CAS No. 2549-07-9 corresponding to a mixture of isomers.
    Advantageously, the 1.3 BAC or the 1.4 BAC used in the BACT unit is a mixture of cis and trans isomers in respective proportions from 0/100 to 100/0, in particular from 75/25 to 25/75.
    Advantageously, the proportion of cis isomer in 1.3 BAC is greater than 60%, preferably greater than 70%, in particular greater than 80%, in particular greater than 90%.
    Advantageously, the proportion of trans isomer in 1.4 BAC is greater than 60%, preferably greater than 70%, in particular greater than 80%, in particular greater than 90%.
    BAC and / or X can be replaced, independently of one another, up to 30 mol% by other diamines defined above, in particular by an aliphatic diamine, linear or branched, a cycloaliphatic diamine or a arylaromatic diamine such as meta-xylene diamine (MXDA).
    As an example, the linear or branched aliphatic diamine is chosen from 1,4butanediamine, 1,5-pentanediamine, 2-methyl-1,5-pentanediamine (MPMD), 1,6 hexanediamine, 1, 8-octanediamine (OMDA), 1,9-nonanediamine (NMDA), Ia2-methyl1,8-octane-diamine (MODA), 2,2,4-trimethylhexamethylenediamine (TMHMD), 2,4,4trimethylhexamethylenediamine (TMHMD ), 5-methyl-1,9-nonanediamine, 1,11undecanediamine, 2-butyl-2-ethyl-1,5-pentanediamine, 1,12-dodecanediamine, 1,13-tridecanediamine, 1,14 -tetradecanediamine, 1,16-hexadecanediamine and 1,18octadecanediamine.
    The cycloaliphatic diamine can be chosen from isophoronediamine, norbornanedimethylamine, 4,4'-diaminodicyclohexylmethane (PACM), 2,2- (4,4'3064271
    -11 diamino-dicyclohexyl) propane (PACP), and 3,3'-dimethyl-4,4'-diaminodicyclohexylethane (MACM).
    T can be replaced up to 30 mol% by other dicarboxylic acids above defined, in particular by other aromatic, aliphatic or cycloaliphatic dicarboxylic acids.
    The aromatic dicarboxylic acids can be chosen from naphthalenedicarboxylic acid (NDA) and isophthalic acid (IPA).
    The aliphatic dicarboxylic acids can be chosen from adipic acid, suberic acid, azelaic acid, sebacic acid, undecanedioic acid, dodecanedioic acid, brassylic acid, tetradecanedioic acid, pentadecanedioic acid, hexadecanedioic acid, octadecanedioic acid and dimerized fatty acids.
    The cycloaliphatic dicarboxylic acids can be chosen from ciset / or trans-cyclohexane-1,4-dicarboxylic acid and / or cis- and / or trans-cyclohexane-1,3dicarboxylic acid (CHDA).
    BAC and / or X and / or T can be replaced, independently of one another, up to 30 mol% by lactams or aminocarboxylic acids.
    The lactams and aminocarboxylic acids can be chosen from caprolactam (CL), α, ω-aminocaproic acid, α, ω-aminononanoic acid, α, ωaminoundecanoic acid (AUA), lauryllactam (LL) and l 'α, ω-aminododecanoic acid (ADA).
    30% by mole maximum, relative to the total sum of the monomers BAC, X and T, of replacement whether by another diamine, another diacid, a lactam or an aminocarboxylic acid or any mixture of these is possible .
    Advantageously, 20% by mole maximum, relative to the total sum of the monomers BAC, X and T, of replacement whether it be by another diamine, another diacid, a lactam or an aminocarboxylic acid or any mixture thereof. is possible.
    Advantageously, 10% by mole maximum, relative to the total sum of the monomers BAC, X and T, of replacement whether it be by another diamine, another diacid, a lactam or an aminocarboxylic acid or any mixture thereof. is possible.
    In an advantageous embodiment, the present invention relates to one of the compositions for thermoplastic material No. 1 to 12 defined below, said composition comprising a semi-crystalline polyamide polymer, optionally short reinforcing fibers, said semi polyamide polymer -crystalline comprising a BACT / XT copolyamide in the proportions defined in Table I below:
    Composition No. Polymerpolyamidesemi-crystalline% in weight Fibers fromshort reinforcement% in weight BACT% molar XT% molar 1 30-100 0-70 > 70-99.1 0.9- <30 2 30-100 0-70 80-99 1-20 3 30-100 0-70 90-99 1-10 4 40-80 0-70 > 70-99.1 0.9- <30 5 40-80 0-70 80-99 1-20 6 40-80 0-70 90-99 1-10 7 30-100 20-60 > 70-99.1 0.9- <30 8 30-100 20-60 80-99 1-20 9 30-100 20-60 90-99 1-10 10 40-80 20-60 > 70-99.1 0.9- <30 11 40-80 20-60 80-99 1-20 12 40-80 20-60 90-99 1-10
    Table I
    Advantageously, the compositions 1 to 12 comprise from 0 to 50% by weight of additives and / or other polymers.
    Advantageously, said compositions consist of a semi-crystalline polyamide polymer, optionally short reinforcing fibers, and from 0 to 50% by weight of additives and / or other polymers, said semi-crystalline polyamide polymer comprising a copolyamide BACT / XT in the proportions defined in Table I.
    Advantageously, said compositions consist of a semi-crystalline polyamide polymer, optionally short reinforcing fibers, and from 0 to 50% by weight of additives and / or other polymers, said semi-crystalline polyamide polymer consisting of '' A BACT / XT copolyamide in the proportions defined in Table I.
    Advantageously, the proportion of additives and / or other polymers in the compositions defined above is more than 0 to 50% by weight.
    Advantageously, in the compositions defined above, X is a C9 diamine,
    C10, C11 and C12, in particular C10, C11 and C12.
    The inventors therefore unexpectedly found that the compositions of the invention exhibited an excellent ability to crystallize, a high Tg and Tf, and
    - 13 especially a higher enthalpy (and therefore higher hot modulus) than the compositions of the prior art.
    In an advantageous embodiment, the present invention relates to a composition as defined above, in which said polycrystalline polyamide polymer has a melting temperature Tf of from 290 ° C to 340 ° C, preferably of from 300 ° C to 330 ° C, more preferably from 310 ° C to 330 ° C, as determined according to ISO 11357-3 (2013).
    In an advantageous embodiment, the present invention relates to a composition as defined above, in which said polycrystalline polyamide polymer has a glass transition temperature Tg> 150 ° C, preferably> 160 ° C, more preferably> 170 ° C, determined according to ISO 11357-2: 2013.
    Advantageously, the Tg is between 155 and 190 ° C.
    In an advantageous embodiment, the present invention relates to a composition as defined above, in which said semi-crystalline polyamide polymer has a difference between the melting temperature and the crystallization temperature Tf-Tc <40 ° C, preferably <30 ° C, determined according to ISO 11357-3: 2013.
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that the enthalpy of crystallization of the semi-crystalline polyamide polymer, measured in Differential Scanning Calorimetry (DSC) according to ISO Standard 11357 -3: 2013, is greater than 40 J / g, preferably greater than 45 J / g, and even more preferably 50J / g.
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that said semi-crystalline polyamide polymer has a melting temperature: Tf comprised from 290 ° C to 340 ° C and a Tg> 150 ° C.
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that said semi-crystalline polyamide polymer has a melting temperature: Tf comprised from 290 ° C to 340 ° C and a Tg> 160 ° C.
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that said semi-crystalline polyamide polymer has a melting temperature: Tf comprised from 290 ° C to 340 ° C and a Tg> 170 ° C.
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that said polyamide polymer
    - 14 semi-crystalline has a melting temperature: Tf between 300 ° C to 330 ° C and a Tg> 150 ° C.
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that said semi-crystalline polyamide polymer has a melting temperature: Tf comprised from 300 ° C to 330 ° C and a Tg> 160 ° C.
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that said semi-crystalline polyamide polymer has a melting temperature: Tf comprised from 300 ° C to 330 ° C and a Tg> 170 ° C.
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that said semi-crystalline polyamide polymer has a melting temperature: Tf comprised from 310 ° C to 330 ° C and a Tg> 150 ° C.
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that said semi-crystalline polyamide polymer has a melting temperature: Tf comprised from 310 ° C to 330 ° C and a Tg> 160 ° C.
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that said semi-crystalline polyamide polymer has a melting temperature: Tf comprised from 310 ° C to 330 ° C and a Tg> 170 ° C.
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that said semi-crystalline polyamide polymer has the following characteristics (Table II):
    Composition No. Compositionsinitials Tf (° C) Tg (° C) Tf-Tc(° C) Delta Hc(J / g) 13 Compositions 1 to 12 290-340 > 150 ° C 14 Compositions 1 to 12 290-340 > 160 ° C 15 Compositions 1 to 12 290-340 > 170 ° C 16 Compositions 1 to 12 300-330 > 150 ° C 17 Compositions 1 to 12 300-330 > 160 ° C 18 Compositions 1 to 12 300-330 > 170 ° C 19 Compositions 1 to 12 310-330 > 150 ° C 20 Compositions 1 to 12 310-330 > 160 ° C
    21 Compositions 1 to 12 310-330 > 170 ° C 22 Compositions 1 to 12 290-340 > 150 ° C <40 23 Compositions 1 to 12 290-340 > 160 ° C <40 24 Compositions 1 to 12 290-340 > 170 ° C <40 25 Compositions 1 to 12 300-330 > 150 ° C <40 26 Compositions 1 to 12 300-330 > 160 ° C <40 27 Compositions 1 to 12 300-330 > 170 ° C <40 28 Compositions 1 to 12 310-330 > 150 ° C <40 29 Compositions 1 to 12 310-330 > 160 ° C <40 30 Compositions 1 to 12 310-330 > 170 ° C <40 31 Compositions 1 to 12 290-340 > 150 ° C <30 32 Compositions 1 to 12 290-340 > 160 ° C <30 33 Compositions 1 to 12 290-340 > 170 ° C <30 34 Compositions 1 to 12 300-330 > 150 ° C <30 35 Compositions 1 to 12 300-330 > 160 ° C <30 36 Compositions 1 to 12 300-330 > 170 ° C <30 37 Compositions 1 to 12 310-330 > 150 ° C <30 38 Compositions 1 to 12 310-330 > 160 ° C <30 39 Compositions 1 to 12 310-330 > 170 ° C <30 40 Compositions 1 to 12 290-340 > 150 ° C <40 > 40 41 Compositions 1 to 12 290-340 > 160 ° C <40 > 40 42 Compositions 1 to 12 290-340 > 170 ° C <40 > 40 43 Compositions 1 to 12 300-330 > 150 ° C <40 > 40 44 Compositions 1 to 12 300-330 > 160 ° C <40 > 40 45 Compositions 1 to 12 300-330 > 170 ° C <40 > 40 46 Compositions 1 to 12 310-330 > 150 ° C <40 > 40 47 Compositions 1 to 12 310-330 > 160 ° C <40 > 40 48 Compositions 1 to 12 310-330 > 170 ° C <40 > 40 49 Compositions 1 to 12 290-340 > 150 ° C <30 > 40 50 Compositions 1 to 12 290-340 > 160 ° C <30 > 40 51 Compositions 1 to 12 290-340 > 170 ° C <30 > 40 52 Compositions 1 to 12 300-330 > 150 ° C <30 > 40 53 Compositions 1 to 12 300-330 > 160 ° C <30 > 40 54 Compositions 1 to 12 300-330 > 170 ° C <30 > 40 55 Compositions 1 to 12 310-330 > 150 ° C <30 > 40
    56 Compositions 1 to 12 310-330 > 160 ° C <30 > 40 57 Compositions 1 to 12 310-330 > 170 ° C <30 > 40 58 Compositions 1 to 12 290-340 > 150 ° C <40 > 45 59 Compositions 1 to 12 290-340 > 160 ° C <40 > 45 60 Compositions 1 to 12 290-340 > 170 ° C <40 > 45 61 Compositions 1 to 12 300-330 > 150 ° C <40 > 45 62 Compositions 1 to 12 300-330 > 160 ° C <40 > 45 63 Compositions 1 to 12 300-330 > 170 ° C <40 > 45 64 Compositions 1 to 12 310-330 > 150 ° C <40 > 45 65 Compositions 1 to 12 310-330 > 160 ° C <40 > 45 66 Compositions 1 to 12 310-330 > 170 ° C <40 > 45 67 Compositions 1 to 12 290-340 > 150 ° C <30 > 45 68 Compositions 1 to 12 290-340 > 160 ° C <30 > 45 69 Compositions 1 to 12 290-340 > 170 ° C <30 > 45 70 Compositions 1 to 12 300-330 > 150 ° C <30 > 45 71 Compositions 1 to 12 300-330 > 160 ° C <30 > 45 72 Compositions 1 to 12 300-330 > 170 ° C <30 > 45 73 Compositions 1 to 12 310-330 > 150 ° C <30 > 45 74 Compositions 1 to 12 310-330 > 160 ° C <30 > 45 75 Compositions 1 to 12 310-330 > 170 ° C <30 > 45 76 Compositions 1 to 12 290-340 > 150 ° C <40 > 50 77 Compositions 1 to 12 290-340 > 160 ° C <40 > 50 78 Compositions 1 to 12 290-340 > 170 ° C <40 > 50 79 Compositions 1 to 12 300-330 > 150 ° C <40 > 50 80 Compositions 1 to 12 300-330 > 160 ° C <40 > 50 81 Compositions 1 to 12 300-330 > 170 ° C <40 > 50 82 Compositions 1 to 12 310-330 > 150 ° C <40 > 50 83 Compositions 1 to 12 310-330 > 160 ° C <40 > 50 84 Compositions 1 to 12 310-330 > 170 ° C <40 > 50 85 Compositions 1 to 12 290-340 > 150 ° C <30 > 50 86 Compositions 1 to 12 290-340 > 160 ° C <30 > 50 87 Compositions 1 to 12 290-340 > 170 ° C <30 > 50 88 Compositions 1 to 12 300-330 > 150 ° C <30 > 50 89 Compositions 1 to 12 300-330 > 160 ° C <30 > 50 90 Compositions 1 to 12 300-330 > 170 ° C <30 > 50
    91 Compositions 1 to 12 310-330 > 150 ° C <30 > 50 92 Compositions 1 to 12 310-330 > 160 ° C <30 > 50 93 Compositions 1 to 12 310-330 > 170 ° C <30 > 50
    Table II
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that the BAC is 1,3 BAC.
    Advantageously, 1,3 BAC is a mixture of cis and trans isomers in respective proportions from 0/100 to 100/0, in particular from 75/25 to 25/75.
    Advantageously, the proportion of cis isomer in 1.3 BAC is greater than 60%, preferably greater than 70%, in particular greater than 80%, in particular greater than 90%.
    In an advantageous embodiment, the present invention relates to a composition as defined above, in which the BAC is 1.3 BAC and XT is chosen from 9T, 10T, 11T and 12T, more preferably 10T, 11T and 12T .
    Advantageously, XT is 11T or 12T.
    Advantageously, XT is 10T, 10 corresponding to 1.10 decanediamine.
    In an advantageous embodiment, the present invention relates to a composition as defined above, in which the sum of the monomers which replace terephthalic acid, BAC and X is equal to 0. In this latter embodiment, it there is therefore no longer any possible substitution of the monomers in compositions 1 to 93 as defined above.
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that said semi-crystalline polyamide polymer is a non-reactive composition according to b).
    This means that said composition is the same as that of the matrix polymer (polyamide) of said thermoplastic material because there is no reaction in this composition, which remains stable and non-evolutive in terms of molecular weight when it is heated for setting work of the thermoplastic material of the invention. The characteristics of the polyamide polymer in this composition are the same, with Tf, Tg, Tf-Tc and Delta Hc as defined above as those of the final polymer.
    The polyamides according to b) are obtained by conventional polycondensation reaction from the monomer components which are diamines, diacids and optionally amino acids or lactams, in particular in the context of substitution of the monomers.
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that said composition
    - 18polyamide is a reactive prepolymer composition according to a) and precursor of said polyamide polymer of said matrix of the thermoplastic material.
    Depending on the reactive composition a), three possibilities can be distinguished below:
    Advantageously, said composition a) comprises or consists of at least one reactive prepolymer carrying on the same chain of two terminal functions X 'and Y', respectively co-reactive functions with one another by condensation, with X and Y 'being amine and carboxyl or carboxyl and amine respectively.
    The prepolymer is a reactive polyamide carrying on the same chain (that is to say on the same prepolymer) of two terminal functions X and Y ’respectively coreactive functions between them by condensation.
    This condensation (or polycondensation) reaction can cause the elimination of by-products. These can be removed preferably by working in a process using open mold technology. In the case of a closed mold process, a degassing step, preferably under vacuum, of the by-products eliminated by the reaction is present, this in order to avoid the formation of microbubbles of the by-products in the final thermoplastic material , which (microbubbles) can affect the mechanical performance of the material if they are not eliminated in this way.
    The term "reactive" therefore means that the Mn of the prepolymer evolves by more than 50% after reaction on itself or with another prepolymer or else by chain extension.
    After condensation, the characteristics of the final polyamide polymer obtained in this composition are the same, with Tf, Tg, Tf-Tc and Delta Hc as defined above.
    Advantageously, said reactive composition a) comprises at least two polyamide prepolymer reactive with each other and each carrying two identical terminal functions X or Y ', said function X of a prepolymer being able to react only with said function Y' of the other prepolymer , in particular by condensation, more particularly with X 'and Y' being amine and carboxyl or carboxyl and amine respectively.
    Likewise, this condensation (or polycondensation) reaction can cause the elimination of by-products which can be eliminated as defined above.
    After condensation, the characteristics of the final polyamide polymer obtained in this composition are the same, with Tf, Tg, Tf-Tc and Delta Hc as defined above.
    Advantageously, said composition a) or precursor composition comprises or consists of:
    - 19a1) at least one prepolymer of said thermoplastic polyamide polymer, carrying n terminal reactive functions X ′, chosen from: -NH2, -CO2H and -OH, preferably NH 2 and -CO 2 H with n being 1 to 3, of preferably from 1 to 2, more preferably 1 or 2, more particularly 2 a2) at least one chain extender Y-A'-Y, with A 'being a hydrocarbon biradical, of non-polymeric structure, carrying 2 terminal reactive functions Y identical, reactive by polyaddition with at least one function X 'of said prepolymer a1), preferably of molecular mass less than 500, more preferably less than 400.
    As suitable examples of extenders a2) as a function of the functions X ′ carried by said semi-crystalline polyamide prepolymer a1), the following may be mentioned:
    when X 'is NH 2 or OH, preferably NH 2 : o either the chain extender Y-A'-Y corresponds to
    Y chosen from the groups: maleimide, optionally blocked isocyanate, oxazinone, oxazolinone and epoxy, and
    A ’is a hydrocarbon spacer optionally comprising one or more heteroatoms, and connecting the functions Y to each other, in particular A’ is a hydrocarbon spacer or a carbon radical carrying the reactive functions or groups Y, chosen from:
    • a covalent bond between two functions (groups) Y in the case where Y = oxazinone and oxazolinone or • an aliphatic hydrocarbon chain or an aromatic and / or cycloaliphatic hydrocarbon chain, the latter two comprising at least one ring of 5 or 6 atoms of optionally substituted carbon, optionally with said aliphatic hydrocarbon chain optionally having a molecular weight of 14 to 400 g.mol ' 1 o or the chain extender Y-A'-Y corresponds to Y being a caprolactam group and to A' can be a carbonyl radical such as carbonyl biscaprolactam or A 'which can be a terephthaloyl or an isophthaloyl, where either said chain extender Y-A'-Y carries a group Y of cyclic anhydride and preferably this extender is chosen from a dianhydride cycloaliphatic and / or aromatic carboxylic acid and more preferably it is chosen from: ethylene tetracarboxylic dianhydride, pyromelliti dianhydride that, 3,3 ', 4,4'-biphenyltetracarboxylic dianhydride, 1,4,5,8naphthalene tetracarboxylic dianhydride, perylenetetracarboxylic dianhydride,
    -20dianhydride 3.3 ', 4,4'-benzophenone tetracarboxylic, 1,2,3,4cyclobutanetetracarboxylic dianhydride, hexafluoroisopropylidene bisphthalic dianhydride, 9,9-bis (trifluoromethyl) xanthenetetracarboxylic dianhydride, 3.3' dianhydride , 4'-diphenylsulfonetetracarboxylic, bicyclo dianhydride [2.2.2] oct-7-ene-2,3,5,6-tetracarboxylic, 1,2,3,4 dianhydride, cyclopentanetetracarboxylic, 3.3 'dianhydride, 4,4 '-diphenyl ether tetracarboxylic or mixtures thereof and when X' is COOH:
    o said chain extender Y-A’-Y corresponds to:
    Y chosen from groups: epoxy, oxazoline, oxazine, imidazoline or aziridine, such as 1, l'-iso- or terephthaloyl-bis (2-methyl aziridine)
    A ’being a carbonaceous (radical) spacer as defined above.
    More particularly, when in said Y-A'-Y extender, said Y function is chosen from oxazinone, oxazolinone, oxazine, oxazoline or imidazoline, in this case, in the chain extender represented by Y-A'-Y, A ' may represent an alkylene such as- (CH 2 ) m with m ranging from 1 to 14 and preferably from 2 to 10 or A ′ may represent a cycloalkylene and / or a substituted (alkyl) or unsubstituted arylene, such as benzene arylenes, such as the phenylenes o-, m-, -p or the naphthalene arylenes and preferably A ′ is an arylene and / or a cycloalkylene.
    In the case of carbonyl- or terephthaloyl- or isophthaloyl- biscaprolactam as chain extender Y-A'-Y, the preferred conditions avoid the elimination of by-product, such as caprolactam during said polymerization and use in melted state.
    In the possible case cited above where Y represents a blocked isocyanate function, this blocking can be obtained by blocking agents of the isocyanate function, such as epsilon-caprolactam, methyl ethyl ketoxime, dimethyl pyrazole, di ethyl malonate.
    Likewise, in the case where the extender is a dianhydride reacting with a prepolymer P (X ') n where X' = NH 2 , the preferred conditions avoid any formation of imide ring during the polymerization and during the implementation at the molten state.
    As examples of chain extenders with reactive function Y = epoxy which are suitable and which are suitable for carrying out the invention, mention may be made of optionally substituted aliphatic, cycloaliphatic or aromatic diepoxides. As examples of aliphatic diepoxides, mention may be made of diglycidyl ethers of aliphatic diols, as aromatic diepoxides of diglycidyl ethers of bisphenol A (DGEBA diglycidyl ether) and as cycloaliphatic diepoxides of bisolipol diol ethers or cycloaliphatic diol ethers Has hydrogenated. In a more
    -21 general, as suitable examples of diepoxides according to the invention, there may be mentioned bisphenol A diglycidyl ether (DGEBA) and its hydrogenated derivative (cycloaliphatic), bisphenol F diglycidyl ether, tetrabromo bisphenol A diglycidyl ether or hydroquinone diglycidyl ether, ethylene glycol diglycidyl ether, propylene glycol diglycidyl ether, butylene glycol diglycidyl ether, neopentyl glycol diglycidyl ether, 1,4-butanediol diglycidyl ether, 1,6hexanediol diglycidyl ether, cyclohexanedimethanol diglycidyl ether, polyethylene glycol diglycidyl ether ether of Mn <500, polytetramethylene glycol diglycidyl ether of Mn <500, resorcinol diglycidyl ether, neopentylglycol diglycidyl ether, bisphenol A polyethylene glycol diglycidyl ether of Mn <500, bisphenol A polypropylene glycol diglycidyl ether of Mn <500 that the tere acid glycidyl ester phthalic or epoxidized diolefins (dienes) or fatty acids with epoxidized ethylenic double unsaturation, diglycidyl 1,2 cyclohexane dicarboxylate and mixtures of the above-mentioned diepoxides.
    As examples of chain extenders carrying reactive functions Y oxazoline or oxazine suitable for the implementation of the invention, reference may be made to those described under references "A", "B", "C" and "D" on page 7 of application EP 0 581 642, as well as their preparation processes and their reaction modes which are exposed therein. "A" in this document is bisoxazoline, "B" bisoxazine, "C" 1,3 phenylene bisoxazoline and "D" 1,4-phenylene bisoxazoline.
    As examples of chain extenders with reactive function imidazoline Y suitable for implementing the invention, reference may be made to those described (“A” to “F”) on pages 7 to 8 and table 1 of the page 10 in application EP 0 739 924 as well as their preparation methods and their reaction modes which are exposed therein.
    As examples of chain extenders with reactive function Y = oxazinone or oxazolinone which are suitable for implementing the invention, reference may be made to those described under references "A" to "D" on page 7 to 8 of EP 0 581 641, as well as their preparation processes and their reaction methods which are exposed therein.
    As examples of suitable Y groups oxazinones (6 atom ring) and oxazolinones (5 atom ring), mention may be made of Y groups derived from: oxazinone or oxazolinone benzoxazinone, with the spacer A ′ possibly being a single bond covalent with respective corresponding extenders being: bis (benzoxazinone), bisoxazinone and bisoxazolinone. A 'can also be a C1 to C14 alkylene, preferably C 2 to C 10 but preferably A' is an arylene and more particularly it can be a phenylene (substituted by Y in positions 1,2 or 1,3 or 1 , 4) or a naphthalene radical (disubstituted by Y) or a phthaloyl (iso- or terephthaloyl) or A ′ can be a cycloalkylene.
    For the Y functions such as oxazine (cycle to 6), oxazoline (cycle to 5) and imidazoline (cycle to 5), the radical A 'can be as described above with A' possibly being a single covalent bond and with the respective corresponding extenders being: bisoxazine, bisoxazoline and bisimidazoline. A ’can also be a C1 to C14 alkylene, preferably a C2 to C10 alkylene. The radical A ′ is preferably an arylene and, more particularly, it can be a phenylene (substituted by Y in positions 1,2 or 1,3 or 1,4) or a naphthalene radical (disubstituted by Y) or a phthaloyl ( iso- or terephthaloyl) or A 'can be a cycloalkylene.
    In the case where Y = aziridine (nitrogen heterocycle with 3 atoms equivalent to ethylene oxide by replacing the ether -O- by -NH-), the radical A 'can be a phthaloyl (1,1'iso or tere - phthaloyl) with an example of an extender of this type, 1, 1 'isophthaloyl-bis (2methyl aziridine).
    The presence of a catalyst for the reaction between said prepolymer P (X ') n and said extender Y-A'-Y at a rate ranging from 0.001 to 2%, preferably from 0.01 to 0.5% relative to to the total weight of two co-reactants mentioned can accelerate the (poly) addition reaction and thus shorten the production cycle.
    According to a more specific case of the choice of said extender, A ′ may represent an alkylene, such that - (CH2) m-with m ranging from 1 to 14 and preferably from 2 to 10 or represents a substituted or alkyl substituted arylene, such as benzene arylenes (such as phenylen o-, m-, -p) or naphthalenic (with arylenes: naphthalenylenes). Preferably, A ′ represents an arylene which may be benzene or naphthenic substituted or not.
    As already specified, said chain extender (a2) has a non-polymeric structure and preferably a molecular mass less than or equal to 500, more preferably less than or equal to 400.
    Said reactive prepolymers of said reactive composition a), according to the three options mentioned above, have a number average molecular mass Mn preferably ranging from 500 to 20,000, in particular from 500 to 10,000, in particular 1,000 to 6,000. All the masses Mn are determined by potentiometry or by NMR (Postma et al. (Polymer, 47, 18991911 (2006)).
    In the case of the reactive compositions of the invention according to definition a), said reactive prepolymers are prepared by conventional polycondensation reaction between the corresponding diamine and diacid components and optionally (depending on the substitutions) amino acids or lactams. The prepolymers carrying X 'and Y' amine and carboxyl functions on the same chain can be obtained for example by adding a combination of monomers (amino acid, diamine, diacid) having in total an equal amount of amine and carboxyl units, but not not driving the reaction up
    -23 total conversion. Another way of obtaining these prepolymers carrying a function X 'and a Y' is, for example, by combining a prepolymer carrying 2 identical functions X '= amine, with a diacid prepolymer carrying Y': carboxyl, with an overall molar level of acid functions equal to that of the starting X 'amine functions.
    To obtain prepolymers functionalized with identical functions (amines or carboxyl) on the same chain, it suffices to have an excess of diamine (or of amine functions overall) to have terminal amine functions or excess of diacid (or of carboxyl functions globally) to have carboxyl terminal functions.
    In the case of a prepolymer P (X ') n with n identical X' functions, functionality 1 can be obtained in the presence of a blocking monofunctional component (monoacid or monoamine depending on the nature of X '= amine or carboxyl ).
    A functionality n = 2 can be obtained from difunctional components: diamines and diacids with excess of one to fix X ’as a function of this excess.
    For n = 3 for example, for a prepolymer P (X ') n, the presence of a trifunctional component is required, for example the presence of a triamine (one mole per chain of prepolymer) with a diamine in the reaction with a diacid. The preferred functionality for P (X ’) n is n = 2.
    In an advantageous embodiment, the present invention relates to a composition as defined above, said composition a) or precursor composition, comprising or consisting of:
    a1) at least one prepolymer of said thermoplastic polyamide polymer, carrying n terminal reactive functions X ', and a2) at least one chain extender Y-A'-Y, in which X' is NH 2 or OH, in particular NH 2 and Y is chosen from an anhydride, in particular dianhydride 3,3 ', 4,4'-benzophenone tetracarboxylic, an oxazinone, an oxazolinone and an epoxy
    In an advantageous embodiment, the present invention relates to a composition as defined above, said composition a) or precursor composition, comprising or consisting of:
    a1) at least one prepolymer of said thermoplastic polyamide polymer, carrying n terminal reactive functions X ', and a2) at least one chain extender Y-A'-Y, in which X' is CO 2 H and Y is chosen from a epoxy and an oxazoline.
    Advantageously, X 'is CO2H and Y-A'-Y is chosen from phenylenes bis oxazolines, preferably 1,3-phenylene-bis (2-oxazoline) or 1,4-phenylene-bis (2oxazoline) ( PBO).
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that it comprises a1) at least one amino prepolymer (carrying -NH2), of said thermoplastic polymer of the matrix , in particular with at least 50% and more particularly with 100% of the end groups of said prepolymer a1) being functions of primary amine -NH2 and a2) at least one chain extender, non-polymeric and carrying a carboxylic anhydride group cyclic, preferably carried by an aromatic ring, having as a substituent a group comprising an ethylenic or acetylenic unsaturation, preferably acetylenic, said carboxylic anhydride group possibly being in acid, ester, amide or imide form with said extender a2) being present at a rate corresponding to a molar ratio a2) / (- NH2) of less than 0.36, preferably ranging from 0.1 to 0.35, more preferably ranging from 0.15 to 0.35 and even more preferably ranging from 0.15 to 0.31 and in that said thermoplastic polymer of the matrix is the product of the polymerization reaction by elongation of said prepolymer a1) by said a2).
    Said reaction by the choice of components a1) and a2) and their specific molar ratio leads to a final thermoplastic polymer which is not crosslinked.
    Said prepolymer a 1) carries primary amine groups represented by -NH2. More particularly, it should be noted that the average number of primary amine groups per prepolymer molecule a1), in other words the average functionality in primary amine groups, can vary from 1 to 3 and preferably from 1 to 2. In particular, the functionality of said prepolymer a1) of at least 50% of the end groups of said prepolymer a1) being functions of primary amine -NH2, this means that it is possible that some of them are carboxyl groups or chain ends blocked without a group reactive and in this case, the average functionality in -NH2 can thus vary from 1 to 3 and preferably from 1 to 2.
    The term "thermoplastic" in the case of the present invention means that the polymer resulting from the reaction of the prepolymer a1) and of the extender a2) is essentially thermoplastic, which means that it contains less than 15% of its weight , preferably less than 10% of its weight and more preferentially less than 5% of its weight and even more preferentially 0% of its weight (to within 0.5% or within 1%) of crosslinked polymers which are insoluble or infusible .
    Said extender a2) can be chosen from:
    -25- anhydrides and anhydride derivatives in acid, ester, amide or imide form of ethynyl o-phthalic, methyl ethynyl o-phthalic, phenyl ethynyl o-phthalic, naphthyl ethynyl o-phthalic, 4- (o-phthaloyl ethynyl ) o-phthalic or 4- (phenyl ethynyl ketone) o-phthalic, the latter also being called 4- (phenyl ethynyl) trimellitic,
    - the acids or esters or amides of ethynyl isophthalic acids, methyl ethynyl isophthalic, phenyl ethynyl isophthalic, naphthyl ethynyl isophthalic, 4- (o-phthaloyl ethynyl) isophthalic, 4- (phenyl ethynyl ketone) isophthalic, ethyl terephthalic, ethyl terephthalic phenyl ethynyl terephthalic, naphthyl ethynyl terephthalic, 4- (ophthaloyl ethynyl) terephthalic, ethynyl benzoic, methyl ethynyl benzoic, phenyl ethynyl benzoic, naphthyl ethynyl benzoic, 4- (o-phthaloyl ethynyl).
    Advantageously, said extender a2) is chosen from aromatic anhydride compounds, preferably o-phthalic, substituted in position 4 of the aromatic ring by a substituent defined by a group R-C5C- (R ') x- with R being an alkyl in C1-C2 or H or aryl, in particular phenyl or R is the residue of an aromatic carboxylic anhydride, preferably o-phthalic, linked to the acetylenic triple bond by the carbon in position 4 of the aromatic ring and x being equal to 0 or to 1 and for x being equal to 1, R 'being a carbonyl group.
    Advantageously, said extender a2) is chosen from aromatic o-phthalic anhydride compounds carrying in position 4 a substituent group chosen from methyl ethynyl, phenyl ethynyl, 4- (o-phthaloyl) ethynyl, phenyl ethynyl ketone also called phenyl ethynyl anhydride trimellitic and preferably carriers in position 4 of a substituent group chosen from methyl ethynyl and phenyl ethynyl ketone.
    Advantageously, said extender a2), as defined above and whatever its structure, has a molecular weight less than or equal to 500, preferably less than or equal to 400.
    Advantageously, the level of said extender a2), as defined above and whatever its structure, in the said polyamide polymer varies from 1 to 20%, in particular from 5 to 20%.
    In an advantageous embodiment, the present invention relates to a composition as defined above, characterized in that it is a molding composition.
    According to another aspect, the present invention relates to a process for manufacturing a thermoplastic material, in particular a mechanical part or a structural part based on said material, of composition as defined above, characterized in that that it comprises at least one step of polymerization of at least one reactive composition a) as defined above according to the invention or a step of molding or implementation
    At least one non-reactive composition b) as defined above, by extrusion, injection or molding.
    In an advantageous embodiment, the present invention relates to a process for manufacturing a thermoplastic material as defined above, characterized in that it comprises the following steps:
    i) injection of a composition as defined above, optionally devoid of fibrous reinforcement, into an open or closed mold or out of mold, ii) polymerization reaction in the case of a reactive composition a) of polyamide as defined above, by heating said composition of step i) with chain extension, as the case may be, by polycondensation reaction or by polyaddition reaction, in bulk in the molten state, with optionally in the case of polycondensation elimination in a vacuum of the condensation products when it is a closed mold, using a vacuum extraction system, otherwise and preferably with the polycondensation being carried out in an open mold or outside the mold, iii) processing or molding of said composition from step i) in the case of a non-reactive polyamide composition b) to form the final part in a mold or with another processing system and, in the case of a reactive composition a), a processing step by molding or by another processing system and simultaneously with step ii) of polymerization.
    According to another aspect, the present invention relates to a semi-crystalline polyamide polymer, characterized in that it corresponds to (or is the) polymer of the thermoplastic matrix of said thermoplastic material, as defined above, said polymer being a non-reactive polymer as defined according to said composition b) or a polymer capable of being obtained from a reactive composition as defined according to said composition a).
    This thermoplastic polymer is by definition one of the essential components of the composition of the thermoplastic material of the present invention and therefore forms part of the invention as a product linked to the present invention with the same common inventive concept facing the same technical problem to be solved. The invention therefore also covers the use of said thermoplastic polymer according to the invention as a thermoplastic matrix of a thermoplastic material based on a fibrous reinforcement as described above.
    According to yet another aspect, the present invention relates to the use of a composition as defined above or of a non-reactive polymer as defined according to said composition b) or a polymer capable of being obtained from a reactive composition as defined according to said composition a), for the manufacture of mechanical or structural parts, based on said thermoplastic material, of monolayer or multilayer pipe, or of film
    In an advantageous embodiment, the present invention relates to the use as defined above, characterized in that said mechanical or structural parts of said thermoplastic material relate to applications in the automotive, rail, marine (maritime) field ), wind, photovoltaic, solar, including solar panels and components of solar power plants, sports, aeronautics and space, road transport (for trucks), building, civil engineering, panels and leisure.
    According to another aspect, the present invention relates to a thermoplastic material resulting from the use of at least one composition defined above.
    In another advantageous embodiment, the present invention relates to the use as defined above, characterized in that said mechanical parts for applications in the automobile are parts under the engine cover for transporting fluid, in particular in air intake, cooling (for example air, coolant, etc.), transport or transfer devices for fuels or fluids, in particular oil, water, etc.
    In yet another advantageous embodiment, the present invention relates to the use as defined above, characterized in that said mechanical or structural parts for applications in electrical or electronics are goods of electrical and electronic equipment, such as encapsulated solenoids, pumps, telephones, computers, printers, fax machines, modems, monitors, remote controls, cameras, circuit breakers, electrical cable sheaths, fiber optics, switches, multimedia systems.
    Methods for determining the cited characteristics
    - The measurement of intrinsic or inherent viscosity is carried out in m-cresol. The method is well known to those skilled in the art. We follow the ISO 307: 2007 standard but by changing the solvent (use of m-cresol instead of sulfuric acid and the temperature being 20 ° C).
    - The glass transition temperature Tg is measured using a differential scanning calorimeter (DSC), after a second heating pass, according to ISO 113572: 2013. The heating and cooling rate is 20 ° C / min.
    - The melting temperature Tf and the crystallization temperature Te are measured by DSC, according to ISO standard 11357-3: 2013. The heating and cooling rate is 20 ° C / min.
    -28- The enthalpy of crystallization of said matrix polymer is measured in Differential Scanning Calorimetry (DSC) according to standard ISO 11357-3: 2013.
    Examples
    A - Preparation of a polyamide polymer by direct route (without chain extension)
    The following procedure is an example of a preparation process, and is not limiting. It is representative of all the compositions according to the invention:
    5 kg of the following raw materials are introduced into an autoclave reactor of 14 liters:
    500 g of water, the diamines, the amino acid (optionally), the terepthalic acid and optionally one or other diacids, the monofunctional chain regulator: benzoic acid in an amount suitable for the
    Mn target and variant (benzoic acid) from 50 to 100 g, g of sodium hypophosphite in solution,
    0.1 g of WACKER AK1000 defoamer (company Wacker Silicones).
    The nature and molar ratios of the units and molecular structures of the polyamides (by referenced test) are given in Table III below.
    The closed reactor is purged of its residual oxygen and then heated to a temperature of 230 ° C. relative to the material introduced. After 30 minutes of stirring under these conditions, the pressurized vapor which has formed in the reactor is gradually expanded in 60 minutes, while gradually increasing the material temperature so that it becomes established at Tf + 10 ° C at atmospheric pressure.
    The polymerization is then continued under a nitrogen flush of 20 l / h until a viscous polymer is obtained.
    The polymer is then drained by the bottom valve then cooled in a water tank and then put in the form of granules.
    The results are presented in Tables III and IV below. These were obtained from 1.3 BACs with a cis / trans ratio of 75/25 mol%.
    Ref. 10T BACT Tf You Tf-Tc DeltaHc Tg mol% mol% ° c ° C ° C J / g ° c VS10T * 100.0 0.0 314 279 35 63 120
    11 16.7 83.3 314.9 291.2 23.7 58.3 176.1 vsBACT * 0.0 100.0 349 - - - 187
    C denotes Comparative I denotes Invention * According to JP2015017177
    TABLE III
    The results of Table III show that for a molar fraction of BACT of more than 70% to 99.1 mol%, the melting temperature is between 290 ° C and 340 ° C.
    At the same time, the Tg is very high and can be modulated from 155 ° C (not shown in the table) to around 190 ° C.
    Ref. Test type Molecular structure / Molar composition Tf You Tf-Tc DeltaHc Tg Viscositeinherentente ° c ° C ° C J / g ° C C1 Comparative,(EP1988113) 10T / 6T (59/41) 281 236 45 44 122 1.12 C2 Comparative,(EP1988113) 10T / 6T / 11 (60/24/16) 269 220 49 39 111 1.25 C3 Comparative,(WO2011 / 003 93) 10T / TMDT(59/41) 263 197 66 35 133 1.15 C10T Comparative 10T (100) 314 279 35 63 120 insolentuble C4 Comparative 10T / 11 (67/33) 269 232 37 50 84 1.19 C5 Comparative 10.T / 11 (59/41) 261 213 48 39 78 1.15 C6 Comparative 10T / 10I (67/33) 269 205 64 32 110 1.12 C7 Comparative MXDT / 11 (59/41) 211 (*) >100 12 111 1.25 C8 Comparative MPMDT / 11 (59/41) - (*) - - 84 1.14 C9 Comparative 10T / MXDT (50/50) 262 211 51 17 137 0.99 C10 Comparative 10T / MPMDT (59/41) 264 219 45 40 126 1.11 C11 Comparative 10T / MPMDT (50/50) 245 185 60 22 127 1.12 C12 Comparative 10T / 12T / 11 (60/24/16) 271 246 25 56 105 0.98 C13 Comparative 18T / MXDT (71/29) 264 242 22 47 95 0.86 C14 Comparative 1.3BACT / 10T (60/40) 275.6 241.7 33.9 60.8 134.0 0.92 C15 Comparative 1.3BACT / 10T (60/40) 281.7 248.3 33.4 53.5 153.4 1.05 C16 Comparative 1.3BACT / 10T (45/55) 279.4 242.5 36.9 55.5 146.0 0.93 C17 Comparative 1.3BACT / 10T (45/55) 279.8 252.0 27.8 62.2 142.7 0.87 C18 Comparative 1.3BACT / 10T (40/60) 282.0 253.5 28.5 49.7 160.2 1.09 C19 Comparative 1.3BACT / 10T (40/60) 286.1 250.4 35.7 57.0 163.9 0.94
    (*): No crystallization on cooling.
    -30 TABLE IV
    The results of Table IV show that the total substitution of the BAC or of the 10T motif or a proportion of 10T greater than or equal to 30% leads to compositions not exhibiting at least one of the values of Tf, Tg, Tf-Tc and delta Hc required.
    权利要求:
    Claims (23)
    [1]
    1. Composition for thermoplastic material comprising:
    0 to 70% by weight, preferably 20 to 60% by weight, of short reinforcing fibers,
    30 to 100% by weight, preferably 40 to 80% by weight, of a thermoplastic matrix based on at least one semi-crystalline polyamide polymer,
    0 to 50% of additives and / or other polymers, said semi-crystalline polyamide polymer being:
    a) a reactive composition comprising or consisting of, at least one reactive polyamide prepolymer which is a precursor of said semi-crystalline polyamide polymer, or as an alternative to a),
    b) a non-reactive composition of at least one polyamide polymer, said composition being that of said thermoplastic matrix defined above, and said reactive polyamide prepolymer of composition a) and said polyamide polymer of composition b) comprising or consisting of at least one BACT / XT copolyamide in which:
    BACT is an amide unit present at a molar level ranging from more than 70% to 99.1%, preferably from 80 to 99%, more preferably from 90 to 99%, where BAC is chosen from 1,3- bis (aminomethyl) cyclohexyl (1.3 BAC), 1,4-bis (aminomethyl) cyclohexyl (1.4 BAC) and a mixture thereof, and T is terephthalic acid,
    - XT is an amide unit present at a molar level ranging from 0.9 to less than
    30%, preferably from 1 to 20%, more preferably from 1 to 10%, where X is a linear aliphatic diamine at C4 to C18, especially C9 to C18, preferably at C9, C10, C11 and C12, and where T is terephthalic acid, preferably C10, C11 and C12.
    in the BACT and / or XT units, independently of one another, up to 30% by mole, preferably 20% by mole, in particular up to 10% by mole, relative to the total amount of dicarboxylic acids, terephthalic acid can be replaced by other aromatic, aliphatic or cycloaliphatic dicarboxylic acids comprising 6 to 36 carbon atoms, in particular 6 to 14 carbon atoms, and in BACT and / or XT units, independently from each other, up to 30% by mole, preferably 20% by mole, in particular up to 10% by mole, of the BAC
    -32and / or depending on the case of X, relative to the total amount of diamines, can be replaced by other diamines comprising from 4 to 36 carbon atoms, in particular 6 to 12 carbon atoms, and in the copolyamide, not more than 30 mol%, preferably not more than 20%, preferably not more than 10 mol%, based on the total amount of the monomers, may be formed by lactams or aminocarboxylic acids, and provided that the sum of the monomers which replace terephthalic acid, BAC and X does not exceed a concentration of 30% by mole, preferably 20% by mole, preferably 10% by mole, relative to the total amount of monomers used in copolyamide, and provided that BACT and XT units are always present in said polyamide polymer.
    [2]
    2. Composition according to claim 1, in which said semi-crystalline polyamide polymer has a melting temperature Tf of from 290 ° C to 340 ° C, preferably from 300 ° C to 330 ° C, more preferably from 310 ° C to 330 ° C, as determined according to ISO 11357-3 (2013).
    [3]
    3. Composition according to claim 1 or 2, wherein said semi-crystalline polyamide polymer has a glass transition temperature Tg> 150 ° C, preferably> 160 ° C, more preferably> 170 ° C, determined according to ISO 11357 -2: 2013.
    [4]
    4. Composition according to one of claims 1 to 3, in which said semi-crystalline polyamide polymer has a difference between the melting temperature and the crystallization temperature Tf -Te <40 ° C, preferably <30 ° C, determined according to ISO 11357-3: 2013.
    [5]
    5. Composition according to one of claims 1 to 4, characterized in that the enthalpy of crystallization of the semi-crystalline polyamide polymer, measured in Differential Scanning Calorimetry (DSC) according to Standard ISO 11357-3: 2013, is greater at 40 J / g, preferably greater than 45 J / g, more preferably greater than 50 J / g.
    -336. Composition according to one of Claims 1 to 5, characterized in that the BAC is 1.3 BAC.
    [6]
    7. Composition according to one of claims 1 to 6, characterized in that the BAC is 1.3 BAC and XT is chosen from 9T, 10T, 11T and 12T, in particular 10T, 11T and 12T.
    [7]
    8. Composition according to one of claims 1 to 7, characterized in that XT is 10T, 10 corresponding to 1.10 decanediamine.
    [8]
    9. Composition according to one of claims 1 to 8, characterized in that the sum of the monomers which replace terephthalic acid, BAC and X is equal to 0.
    [9]
    10. Composition according to one of claims 1 to 9, characterized in that said composition is a non-reactive composition according to b).
    [10]
    11. Composition according to one of claims 1 to 9, characterized in that said polyamide composition is a reactive prepolymer composition according to a) and precursor of said polyamide polymer of said matrix of the thermoplastic material.
    [11]
    12. Composition according to one of claims 1 to 10, characterized in that it additionally comprises at least one additive.
    [12]
    13. Composition according to claim 12, characterized in that the additive is chosen from an antioxidant, a heat stabilizer, a UV absorber, a light stabilizer, an impact modifier, a lubricant, an inorganic filler, a flame retardant, a nucleating agent and a dye.
    [13]
    14. Composition according to one of claims 1 to 13, characterized in that it is a molding composition.
    [14]
    15. Method for manufacturing a thermoplastic material, in particular a mechanical part or a structural part based on said material, of composition as defined according to one of claims 1 to 13, characterized in that it comprises at least one step of polymerization of at least one reactive composition a) such
    That defined according to claim 9, or a step of molding or using at least one non-reactive composition b) as defined according to claim 9, by extrusion, injection or molding.
    [15]
    16. Method according to claim 15, characterized in that it comprises the following steps:
    i) injection of a composition as defined according to one of claims 1 to 13, optionally devoid of fibrous reinforcement, in an open or closed mold or outside the mold, ii) polymerization reaction in the case of a reactive composition a ) of polyamide according to claim 11, by heating said composition of step i) with chain extension, as the case may be, by polycondensation reaction or by polyaddition reaction, in bulk in the molten state, with optionally in the case of polycondensation, elimination under vacuum of condensation products when it is a closed mold, using a vacuum extraction system, otherwise and preferably with polycondensation being carried out in open mold or out of mold, iii) an implementation or molding of said composition of step i) in the case of a non-reactive polyamide composition b) to form the final part in a mold or with another implementation system and, in the case of a reactive composition a), an implementation step by molding or by another implementation system and simultaneously with step ii) of polymerization.
    [16]
    17. Semi-crystalline polyamide polymer, characterized in that it corresponds to (or is the) polymer of the thermoplastic matrix of said thermoplastic material, as defined according to one of claims 1 to 13, said polymer being a non-reactive polymer as defined according to said composition b) or a polymer capable of being obtained from a reactive composition as defined according to said composition a).
    [17]
    18. Use of a composition as defined according to one of claims 1 to 13 or of a non-reactive polymer as defined according to said composition b) or a polymer capable of being obtained from a reactive composition such as defined according to said composition a), for the manufacture of mechanical or structural parts, based on said thermoplastic material, monolayer or multilayer pipe, or film.
    [18]
    19. Use according to claim 18, characterized in that said mechanical or structural parts of said material relate to applications in the automotive, electrical or electronic, rail, marine, wind, photovoltaic , solar, including solar panels and components of solar power plants, sports, aeronautics and space, road transport (for trucks), building, civil engineering, panels and leisure.
    [19]
    20. Use according to claim 18, characterized in that said mechanical parts for applications in the automobile are parts under an engine hood for transporting fluid, in particular in air intake and cooling devices (for example by air, coolant), transport or transfer of fuels or fluids.
    [20]
    21. Use according to claim 18, characterized in that said mechanical or structural parts for applications in electrical or electronics are goods of electrical and electronic equipment, such as encapsulated solenoids, pumps, telephones, computers, printers, fax machines, modems, monitors, remote controls, cameras, circuit breakers, electrical cable sheaths, fiber optics, switches, multimedia systems.
    [21]
    22. Thermoplastic material characterized in that it results from the use of at least one composition for thermoplastic material as defined according to one of claims 1 to 13.
    [22]
    23. Mechanical or structural part of thermoplastic material, characterized in that it results from the use of at least one composition as defined according to one of claims 1 to 13 or from the use of a polyamide polymer as defined in claim 17 or that it is based on a material as defined in claim 22 or that it is obtained by a process as defined in one of claims 15 or 16.
    [23]
    24. Part according to claim 23, characterized in that they are mechanical parts for applications in the automobile such as parts under engine cover for transporting fluid, in particular in air intake devices , cooling (for example by air, coolant), transport or transfer of fuels or fluids (such as oil, water).
    5 25. Part according to claim 23, characterized in that they are mechanical or structural parts for applications in electrical or electronics such as electrical and electronic equipment goods, such as encapsulated solenoids , pumps, telephones, computers, printers, fax machines, modems, monitors, remote controls, cameras, circuit breakers, electrical cable sheaths, optical fibers,
    10 switches, multimedia systems.
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    同族专利:
    公开号 | 公开日
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    MX2019011097A|2019-11-21|
    KR20190127751A|2019-11-13|
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    法律状态:
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    优先权:
    申请号 | 申请日 | 专利标题
    FR1752485|2017-03-24|
    FR1752485A|FR3064271B1|2017-03-24|2017-03-24|COMPOSITION OF SEMI-CRYSTALLINE POLYAMIDE OF HIGH GLASS TRANSITION TEMPERATURE AND HIGH MELTING TEMPERATURE FOR THERMOPLASTIC MATERIAL, ITS MANUFACTURING PROCESS AND ITS USES|FR1752485A| FR3064271B1|2017-03-24|2017-03-24|COMPOSITION OF SEMI-CRYSTALLINE POLYAMIDE OF HIGH GLASS TRANSITION TEMPERATURE AND HIGH MELTING TEMPERATURE FOR THERMOPLASTIC MATERIAL, ITS MANUFACTURING PROCESS AND ITS USES|
    US16/495,898| US20200024395A1|2017-03-24|2018-03-23|Semi-crystalline polyamide composition having a high glass transition temperature and a high melting temperature for a thermoplastic material, production method thereof and uses of same|
    KR1020197027715A| KR20190127751A|2017-03-24|2018-03-23|Semi-crystalline polyamide compositions having high glass transition temperature and high melting temperature for thermoplastic materials, methods of making and uses thereof|
    JP2019551349A| JP2020512450A|2017-03-24|2018-03-23|Semi-crystalline polyamide compositions with high glass transition temperature and high melting point for thermoplastic materials, process for their production and their use|
    PCT/FR2018/050710| WO2018172717A1|2017-03-24|2018-03-23|Semi-crystalline polyamide composition having a high glass transition temperature and a high melting temperature for a thermoplastic material, production method thereof and uses of same|
    CN201880018705.2A| CN110431169A|2017-03-24|2018-03-23|Semicrystalline polyamides composition, preparation method and its purposes with high glass-transition temperature and high melt temperature for thermoplastic material|
    EP18715788.8A| EP3443022B1|2017-03-24|2018-03-23|Semi-crystalline polyamide composition having a high glass transition temperature and a high melting temperature for a thermoplastic material, production method thereof and uses of same|
    MX2019011097A| MX2019011097A|2017-03-24|2018-03-23|Semi-crystalline polyamide composition having a high glass transition temperature and a high melting temperature for a thermoplastic material, production method thereof and uses of same.|
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