Polydisperse polyamides

A polyamide composition with dispersity greater than 2.25, made from unsorted recyclable materials, addresses the inefficiencies of traditional polyamide recycling by improving mechanical properties and eliminating the need for fine sorting, enhancing market value and reducing waste.

WO2025248208A1PCT designated stage Publication Date: 2025-12-04ARKEMA FRANCE SA
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Patent Information

Application Number
PCT/FR2025/050479
Authority / Receiving Office
WO · WO
Patent Type
Applications
Current Assignee / Owner
Priority Date
2024-05-31
Filing Date
2025-05-28
Publication Date
2025-12-04

AI Technical Summary

Technical Problem

Existing polyamides exhibit high molar mass dispersity, leading to significant waste generation and economic inefficiencies in recycling due to the need for costly and time-consuming sorting, and there is a need for polyamide compositions with improved mechanical properties from recycled materials that require minimal sorting.

Method used

A polyamide composition comprising polyamides with dispersity greater than 2.25, made from unsorted or partially sorted recyclable materials, combining polyamide batches to achieve desired properties, including the use of shock modifiers, plasticizers, and additives, with a focus on aliphatic polyamides and specific molecular structures.

Benefits of technology

The composition achieves improved mechanical properties such as cold shock resistance and fatigue resistance, enabling the use of recycled materials in manufacturing without the need for fine separation, thus enhancing market value and reducing waste.

✦ Generated by Eureka AI based on patent content.

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Abstract

The present invention relates to a polyamide composition comprising, by weight: (a) 35% to 100% of a polyamide component comprising, by weight relative to the total weight of the polyamide component: a. 50% to 95% of at least one polyamide A, b. 5% to 50% of at least one polyamide B different from the polyamide A, (b) 0 to 65% of fillers, (c) 0 to 30% of at least one impact modifier, (d) 0 to 15% of at least one plasticiser, and (e) 0 to 5% of at least one additive, the sum of the constituents (a) to (e) being equal to 100%, in which the polyamide component (a) has a dispersity (D) greater than 2.25, in particular greater than 2.35.
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Description

[0001] DESCRIPTION

[0002] TITLE: POLYDISPERSE POLYAMIDES

[0003] The invention relates to polyamide compositions, their use and their preparation process.

[0004] [Previous technique]

[0005] Polyamides are classically prepared by polycondensation of lactam, amino acid, diamine and dicarboxylic acid, or mixtures thereof. Virgin polyamides prepared in this way generally exhibit, before processing, a molar mass dispersity or polydispersity (D) of between 1.6 and 2.1.

[0006] These polyamides are useful for forming articles shaped by traditional processes such as extrusion, film blowing, or injection molding. These various shaping processes generate a significant amount of waste and production scrap. Furthermore, the shaped articles are discarded after use, forming what is known as "post-consumer" waste. Until now, this waste was most often collected without sorting for disposal through incineration or landfill.

[0007] To avoid depleting the planet's resources and reduce environmental impact, efforts are now focused on maximizing the recycling of production waste and discarded manufactured goods after use. The goal is to recover the polymer and reuse it, for example, in extrusion or injection molding processes. However, recycling presents a significant challenge, particularly the need to separate the various polymers to be recycled in order to obtain a recycled polymer with desirable properties and therefore value. Pre-sorting waste is a time-consuming and costly step that significantly impacts the economic viability of recycling.

[0008] [Summary of the invention]

[0009] There is therefore a need for polyamide compositions, particularly from recycled materials, which have value but require little prior sorting.

[0010] However, it has now been unexpectedly found that compositions comprising several polyamides forming a component with a dispersity (D) greater than 2.25 exhibit improved mechanical properties, particularly in terms of cold shock resistance, yield strength and fatigue resistance, making them particularly interesting for the manufacture of injected parts.

[0011] The present invention therefore relates to a polyamide composition comprising:

[0012] (a) 35 to 100% of a polyamide component comprising, by weight relative to the total weight of the polyamide component: a. 50% to 95% of at least one polyamide A, b. 5% to 50% of at least one polyamide B different from polyamide A,

[0013] (b) from 0 to 65% of charges,

[0014] (c) 0 to 30% of at least one shock modifier,

[0015] (d) 0 to 15% of at least one plasticizer, and

[0016] (e) of 0 to 5% of at least one additive, the sum of constituents (a) to (e) being equal to 100%, wherein said polyamide component (a) has a dispersity (D) greater than 2.25, in particular greater than 2.35, in particular between 2.5 and 15.

[0017] These compositions can be made from unsorted or partially sorted recyclable materials, as a high degree of dispersibility is required, achieved by mixing polyamide batches from various sources. These compositions can therefore be manufactured by combining different polyamide batches to create a composition with desired properties, thus offering significant market value. This allows for the elimination of fine separation of polyamide batches, whether they are objects or production waste.

[0018] Preferably, the polyamide component (a) of the polyamide composition comprises at least 50%, advantageously 75%, preferably 95%, in particular 100% aliphatic polyamide.

[0019] Advantageously, the polyamide component (a) has a C / N ratio greater than or equal to 6.5, in particular greater than or equal to 7.5, especially greater than or equal to 8.5, more particularly greater than or equal to 9.5.

[0020] Furthermore, the polyamide component (a) preferably comprises less than 1000 ppm of catalyst and / or polyamides with non-reactive end-chain functions and / or polyamides with an NH2 / COOH end-chain function ratio greater than 1. Such a polyamide component advantageously allows obtaining a composition free of species resulting from transamidification reactions.

[0021] Preferably, polyamides A and B have an inherent viscosity difference greater than 0.1 dL / g, in particular greater than 0.2 dL / g, especially greater than 0.4 dL / g.

[0022] The polyamide composition advantageously has an inherent viscosity of less than 1.7 dL / g, in particular less than 1.5 dL / g, especially less than 1.3 dL / g.

[0023] Advantageously, the polyamide component (a) comprises at least 30% recycled polyamide. Advantageously, the polyamide component (a) comprises at least 30% by weight of recycled polyamide relative to the total weight of the polyamide component.

[0024] Recycled polyamide preferably contains one or more functional groups resulting from oxidation reactions selected from the following: primary amide, nitrile, methyl end-chain, alkene, formamide, imide, carboxylic acid, and alcohol, in a molar ratio relative to amide functional groups that is higher than that of the same polyamide in a new, unused article. The molar ratio of functional groups resulting from oxidation reactions relative to secondary amide functional groups may range from 0.0001 to 0.3. More specifically, the molar ratio of imide functional groups relative to secondary amide functional groups may range from 0.0005 to 0.02, particularly from 0.001 to 0.08, and especially from 0.005 to 0.05. The molar ratio of carboxylic acid functions to secondary amide functions can range from 0.0005 to 0.02, notably from 0.001 to 0.08, particularly from 0.005 to 0.05.The molar ratio of alcohol functions to secondary amide functions can range from 0.0005 to 0.02, in particular from 0.001 to 0.08, especially from 0.005 to 0.05. The molar ratio of nitrile functions to secondary amide functions can range from 0.0005 to 0.02, in particular from 0.001 to 0.08, especially from 0.005 to 0.05.

[0025] According to a second aspect, the invention aims at the use of such a composition for the manufacture of an article by injection.

[0026] According to a third aspect, the invention relates to a method for preparing a composition comprising the step of:

[0027] (i) mix the components (a) to (e) in a molten state, in particular in an extruder.

[0028] According to a fourth aspect, the invention relates to a method of preparing the composition, in which step (i) is carried out with a residence time of less than five minutes.

[0029] Finally, according to a fifth aspect, the invention relates to a method for implementing such a composition, comprising an extrusion or injection step of said composition at a temperature below 300°C, preferably 280°C. In one embodiment, the method for implementing such a composition comprises an extrusion or injection step of said composition at a temperature ranging from 200°C to 300°C.

[0030] [Definitions]

[0031] Throughout the description, unless otherwise stated, percentages are expressed as a percentage of the total weight of the composition.

[0032] The nomenclature used to designate polyamides is described in ISO 1874-1:2011 "Plastics - Polyamide (PA) materials for molding and extrusion - Part 1: Designation", particularly on page 3 (tables 1 and 2) and is well known to those skilled in the art.

[0033] The term "polyamide" refers to both homopolyamide and copolyamide. By extension, this term also generally refers to copolymers containing amide groups.

[0034] The expression "a polyamide B different from polyamide A" means that polyamide B differs from polyamide A at the level of its molecular structure, in particular by its number-average molecular weight (Mn), its dispersity, the content of end-chain functions and / or its C / N ratio (or average C / N ratio).

[0035] The term "dispersity" refers to the width of the chain length distribution of a polymer. It is given by the ratio between the weight-average molecular mass Mw and the number-average molecular mass Mn. The weight-average molecular masses Mn and Mw are measured by size-exclusion chromatography, in particular by gel permeation chromatography, according to ISO 16014-1:2012, for example according to the following protocol: The polyamide is solubilized at a concentration of 2 g / L in hexafluoroisopropanol stabilized with 0.05 M potassium trifluoroacetate for 24 h at room temperature (20°C).The resulting solution is then filtered through a PTFE membrane with a porosity of 0.2 pm, and then injected at a flow rate of 1 mL / min into a liquid chromatography system equipped with a set of PFG columns from Polymer Standards Service consisting of a pre-column measuring 50 x 8 mm, a 1000 Å column measuring 300 x 8 mm with a particle size of 7 pm, and a 100 Å column measuring 300 x 8 mm with a particle size of 7 pm. Molar masses are measured by the refractive index and are expressed in PMMA equivalents, used as a calibration standard, and then converted to g / mol.

[0036] The term "C / N ratio" refers to the ratio of the number of carbon atoms to nitrogen atoms in a given polyamide unit. When discussing polyamide (or copolyamide) blends, an average C / N ratio is considered, calculated based on the C / N ratio of each constituent of the blend or copolyamide unit, weighted by its respective weight in the blend or copolyamide.

[0037] The average C / N ratio of a polyamide composition can be determined in particular by proton NMR spectroscopy, by dividing the area of ​​the peaks corresponding to the protons of the CH2 groups of the polyamide by the area corresponding to the protons of the NH groups (or possibly the CH2 groups in the alpha position of the amide functions).

[0038] [Detailed description]

[0039] Composition

[0040] According to the invention, the polyamide composition comprises or is made up of, by weight:

[0041] (a) 35% to 100% of a polyamide component comprising, by weight relative to the total weight of the polyamide component: a. 50% to 95%, preferably 55% to 90%, in particular 60% to 85% and especially 70% to 80% of at least one polyamide A, b. 5% to 50%, preferably 10% to 45%, in particular 15% to 40%, and especially 20% to 30% of at least one polyamide B different from polyamide A,

[0042] (b) from 0 to 65%, preferably from 5% to 60%, in particular from 10% to 50%, in particular from 20% to 40% and in particular from 25% to 30% of charges, (c) from 0 to 30%, in particular from 0 to 20% and in particular from 0 to 10% of at least one shock modifier,

[0043] (d) from 0 to 15%, in particular from 0 to 5% and especially from 0 to 1.5% of at least one plasticizer, and

[0044] (e) from 0 to 5%, in particular from 0.1% to 5%, notably from 0.1% to 2% of at least one additive, the sum of constituents (a) to (e) being equal to 100%.

[0045] According to the invention, the polyamide composition comprises, by weight:

[0046] (a) 35% to 100% of a polyamide component comprising, by weight relative to the total weight of the polyamide component: a. 50% to 95%, preferably 55% to 90%, in particular 60% to 85% and especially 70% to 80% of at least one polyamide A, b. 5% to 50%, preferably 10% to 45%, in particular 15% to 40%, and especially 20% to 30% of at least one polyamide B different from polyamide A,

[0047] (b) from 0 to 65%, preferably from 5% to 60%, in particular from 10% to 50%, especially from 20% to 40% and in particular from 25% to 30% of charges,

[0048] (c) from 0 to 30%, in particular from 0 to 20% and especially from 0 to 10% of at least one shock modifier,

[0049] (d) from 0 to 15%, in particular from 0 to 5% and especially from 0 to 1.5% of at least one plasticizer, and

[0050] (e) from 0 to 5%, in particular from 0.1% to 5%, in particular from 0.1% to 2% of at least one additive, the sum of constituents (a) to (e) being equal to 100%, wherein the polyamide component (a) of the composition has a dispersity (D) greater than 2.25, in particular greater than 2.35, in particular between 2.5 and 15.

[0051] Preferably, the polyamide component (a) has a dispersity (D) of 3 to 13, in particular 4 to 12, in particular 5 to 10.

[0052] According to one embodiment, the polyamide composition consists of, by weight:

[0053] (a) 35% to 100% of a polyamide component comprising, by weight relative to the total weight of the polyamide component: a. 50% to 95%, preferably 55% to 90%, in particular 60% to 85% and especially 70% to 80% of at least one polyamide A, b. 5% to 50%, preferably 10% to 45%, in particular 15% to 40%, and especially 20% to 30% of at least one polyamide B different from polyamide A,

[0054] (b) from 0 to 65%, preferably from 5% to 60%, in particular from 10% to 50%, especially from 20% to 40% and in particular from 25% to 30% of charges,

[0055] (c) from 0 to 30%, in particular from 0 to 20% and especially from 0 to 10% of at least one shock modifier,

[0056] (d) from 0 to 15%, in particular from 0 to 5% and especially from 0 to 1.5% of at least one plasticizer, and

[0057] (e) from 0 to 5%, in particular from 0.1% to 5%, notably from 0.1% to 2% of at least one additive, the sum of constituents (a) to (e) being equal to 100%, preferably wherein the polyamide component (a) of the composition exhibits dispersity

[0058] (D) greater than 2.25, in particular greater than 2.35, notably between 2.5 and 15.

[0059] According to one embodiment, the polyamide composition comprises or is made up of, by weight

[0060] (a) 35% to 100% of a polyamide component comprising, by weight relative to the total weight of the polyamide component: a. 50% to 95%, preferably 55% to 90%, in particular 60% to 85% and especially 70% to 80% of at least one polyamide A, b. 5% to 50%, preferably 10% to 45%, in particular 15% to 40%, and especially 20% to 30% of at least one polyamide B other than polyamide A, and

[0061] (b) of more than 0 to 65%, preferably from 5% to 60%, in particular from 10% to 50%, in particular from 20% to 40% and in particular from 25% to 30% of charges,

[0062] (c) from 0 to 30%, in particular from more than 0 to 20% and especially from more than 0 to 10% of at least one shock modifier,

[0063] (d) from 0 to 15%, in particular from more than 0 to 5% and especially from more than 0 to 1.5% of at least one plasticizer, and

[0064] (e) from 0 to 5%, in particular from 0.1% to 5%, in particular from 0.1% to 2% of at least one additive, the sum of constituents (a) to (e) being equal to 100%, preferably wherein the polyamide component (a) of the composition has a dispersity (D) greater than 2.25, in particular greater than 2.35, in particular from 2.5 to 15.

[0065] According to one embodiment, the polyamide composition of the invention does not comprise a semi-aromatic polyamide. According to one embodiment, the polyamide component (a) does not comprise a semi-aromatic polyamide. According to one embodiment, polymer A is not a semi-aromatic polyamide. According to one embodiment, polymer B is not a semi-aromatic polyamide. According to one embodiment, the polyamide composition and / or the polyamide component (a) of the invention does not comprise polyamide 10.T, where 10.T designates a motif obtained from the polycondensation of 1,10-decanediamine and terephthalic acid. According to one embodiment, the polyamide composition of the invention does not comprise a non-crystalline semi-aromatic polyamide. According to one embodiment, the polyamide component (a) does not comprise a non-crystalline semi-aromatic polyamide.In one embodiment, polymer A is not a non-crystalline semi-aromatic polyamide. In another embodiment, polymer B is not a non-crystalline semi-aromatic polyamide. In one embodiment, the polyamide component (a) comprises or is made of a crystalline semi-aromatic polyamide. In one embodiment, polymer A comprises or is made of a crystalline semi-aromatic polyamide. In one embodiment, polymer B comprises or is made of a crystalline semi-aromatic polyamide.

[0066] According to one embodiment, the polyamide composition of the invention comprises or is made up of at least one polyundecanamide (or PA 11 or nylon 11) with an inherent viscosity of 1.53 dL / g, and at least one polyundecanamide (or PA 11 or nylon 11) with an inherent viscosity of 0.96 dL / g, the inherent viscosities each being determined in m-cresol according to ISO 307:2007 but changing the solvent (using m-cresol instead of sulfuric acid and the temperature being 20°C).According to one embodiment, the polyamide composition of the invention comprises or is made up of a polyamide 11 (or polyundecanamide or PA 11 or nylon 11) of inherent viscosity equal to 1.53 dL / g, and a polyamide 11 of inherent viscosity equal to 0.96 dL / g, the inherent viscosities each being determined in m-cresol according to ISO 307:2007 but changing the solvent (using m-cresol instead of sulfuric acid and the temperature being 20°C), said polyamide component (a) having a dispersity equal to 2.7.

[0067] According to one embodiment, the polyamide composition of the invention comprises or is made up of 30% of a polyamide 11 (or polyundecanamide or PA 11 or nylon 11) of inherent viscosity equal to 1.53 dL / g, and 70% of a polyamide 11 of inherent viscosity equal to 0.96 dL / g, the inherent viscosities each being determined in m-cresol according to ISO 307:2007 but by changing the solvent (using m-cresol instead of sulfuric acid and the temperature being 20°C), said polyamide component (a) having a dispersity equal to 2.7.

[0068] According to one embodiment, the polyamide composition of the invention comprises or is made up of 2 to 15 different grades of polyamide 11, preferably from a blend of recycled products, said blend of polyamide 11 having an inherent viscosity of 0.95 dL / g, said inherent viscosity being determined in m-cresol according to ISO 307:2007 but changing the solvent (using m-cresol instead of sulfuric acid and the temperature being 20°C), said polyamide component (a) having a dispersity of 2.5.

[0069] According to one embodiment, the polyamide composition of the invention exhibits excellent impact resistance properties, preferably cold impact resistance. In another embodiment, the polyamide composition of the invention has a notched impact resistance at -30°C within a range of 10 kg / m². 2 at 25 kg / m 2said resistance being determined according to ISO 179-1: 2010 (Charpy impact) on notched specimens of dimensions 80mm x 10mm x 4mm, at a temperature of -30°C + / -2°C on dry samples.

[0070] Polyamide component (a)

[0071] According to the invention, the composition comprises 35% to 100% by weight of polyamide component (a). The polyamide component (a) comprises at least one polyamide A and at least one polyamide B distinct from polyamide A.

[0072] Polyamides A and B respectively comprise or are preferably made up of a repeating motif selected from a motif obtained from the polycondensation of at least one C4-C36 amino acid, a motif obtained from the polycondensation of at least one C4-C36 lactam and an XY motif obtained from the polycondensation of: a diamine, in particular selected from a linear or branched aliphatic diamine, a cycloaliphatic diamine and an aromatic or arylaliphatic diamine or a mixture thereof, and a dicarboxylic acid, in particular selected from an aliphatic diacid, a cycloaliphatic diacid and an aromatic diacid or a mixture thereof, said diamine and said diacid comprising from 4 to 36 carbon atoms respectively.

[0073] In one variant, the repeating motif is obtained by the polycondensation of at least one C4-C aminocarboxylic acid 36, and in particular in C9-C12. Preferably, the aminocarboxylic acid is chosen from 9-aminononanoic acid, 10-aminodecanoic acid, 11-aminoundecanoic acid and 12-aminododecanoic acid, advantageously it is 11-aminoundecanoic acid.

[0074] In a second variant, the repeating motif is obtained by the polycondensation of a lactam at C4-C36, and in particular at C9-C12. Advantageously, the lactam is chosen from decanolactam, undecanolactam, and laurolactam or lauryllactam; preferably, the repeating motif is derived from lauryllactam. According to one embodiment, the repeating motif is obtained by the polycondensation of a lactam at Cg-Ci2, and in particular at C9-C12.

[0075] However, it is perfectly possible to use a mixture of two or more aminocarboxylic acids, a mixture of two or more lactams, or a mixture of one, two, or more aminocarboxylic acids with one, two, or more lactams. More preferably, however, the repeating motif is obtained by polycondensation of a single aminocarboxylic acid or a single lactam.

[0076] In another variant, the polyamide comprises or is made up of a repeating XY pattern.

[0077] The XY repeating motif can be obtained from the polycondensation of a diamine, in particular an aliphatic diamine, linear or branched, a cycloaliphatic diamine, aromatic or arylaliphatic, alone or in a mixture, and at least one dicarboxylic acid, in particular selected from an aliphatic dicarboxylic acid, a cycloaliphatic dicarboxylic acid and an aromatic dicarboxylic acid, alone or in a mixture. Preferably, the XY repeating motif is obtained from the polycondensation of an aliphatic diamine with an aliphatic dicarboxylic acid.

[0078] The said diamine preferably comprises 4 to 36, advantageously 6 to 18, in particular 9 to 18, and especially 6 to 12 carbon atoms.

[0079] The linear aliphatic diamine preferentially corresponds to the formula H2N-(CH2) X -NH2. The linear aliphatic diamine preferentially corresponds to the formula H2N-(CH2) x-NH2 in which x represents a digit or number greater than 0, preferably x is chosen from 1 to 40, preferably from 4 to 36, from 8 to 18, or from 6 to 12. It may be chosen, for example, from butanediamine, pentanediamine, hexanediamine, heptanediamine, octanediamine, nonanediamine, decanediamine, undecanediamine, dodecanediamine, tridecanediamine, tetradecanediamine, hexadecanediamine, octadecanediamine, and octadecenediamine. The linear aliphatic diamines listed may be bio-based as defined in ASTM D6866.

[0080] The branched aliphatic diamine can notably be chosen from 2-methyl-pentanediamine, 2-methyl-1,8-octanediamine or trimethylene (2,2,4 or 2,4,4)hexanediamine.

[0081] The cycloaliphatic diamine can be chosen from those indicated in the publication "Cycloaliphatic Amines" (Encyclopaedia of Chemical Technology, Kirk-Othmer, 4th Edition (1992), pp. 386-405). Preferred are bis(3,5-dialkyl-4-aminocyclohexyl)-methane, bis(3,5-dialkyl-4-aminocyclohexyl)ethane, bis(3,5-dialkyl-4-aminocyclohexyl)-propane, bis(3,5-dialkyl-4-aminocyclo-hexyl)-butane, bis-(3-methyl-4-aminocyclohexyl)-methane or 3'-dimethyl-4,4'-diamino-dicyclohexyl-methane also known as "BMACM" or "MACM" (B), p-bis(aminocyclohexyl)-methane also known as "PACM" (P), isopropylidenedi(cyclohexylamine) (PACP), isophoronediamine (noted IPD) and 2,6-bis(aminomethyl)norbornane (BAMN) or bis(aminomethyl)cyclohexane (BAC).

[0082] For example, arylaliphatic diamine can be chosen from 1,3-xylylene diamine and 1,4-xylylene diamine.

[0083] The dicarboxylic acid preferably comprises 4 to 36, advantageously 6 to 18 and especially 6 to 12 carbon atoms.

[0084] Preferably, the dicarboxylic acid is aliphatic, and in particular linear or branched. A linear aliphatic dicarboxylic acid is especially preferred.

[0085] Linear aliphatic dicarboxylic acid can notably be chosen from succinic acid (4), pentanedioic acid (5), adipic acid (6), heptanedioic acid (7), octanedioic acid (8), azelaic acid (9), sebacic acid (10), undecanedioic acid (11), dodecanedioic acid (12), brassylic acid (13), tetradecanedioic acid (14), hexadecanedioic acid (16), octadecanedioic acid (18), octadecenedioic acid (18), eicosanedioic acid (20), docosanedioic acid (22) and fatty acid dimers containing 36 carbon atoms. The fatty acid dimers mentioned above are dimerized fatty acids obtained by oligomerization or polymerization of long-chain unsaturated monobasic fatty acids (such as linoleic acid and oleic acid), as described in particular in document EP 0 471 566.

[0086] The aromatic dicarboxylic acid can be chosen in particular from terephthalic acid (denoted T), isophthalic acid (denoted I) and a naphthalenic acid (denoted N).

[0087] Preferably, the polyamide component (a) comprises at least 50%, advantageously 75%, preferably 95%, in particular 100% by weight of aliphatic polyamide.

[0088] According to the invention, the polyamide component (a) has a dispersity (D) greater than 2.25. Advantageously, the dispersity (D) of the polyamide component (a) is greater than 2.35, in particular from 2.5 to 15, and more preferably from 3 to 13, in particular from 4 to 12, especially from 5 to 10, preferably from 6 to 9, and most particularly from 7 to 8. In one embodiment, the dispersity (D) of the component (a) is from 2.5 to 5. In another embodiment, the dispersity (D) is from 5 to 7.5. In yet another embodiment, the dispersity (D) is from 7.5 to 10. In yet another embodiment, the dispersity (D) is from 10 to 12.5. According to another embodiment, the dispersion (D) is between 12.5 and 15.

[0089] Advantageously, the polyamide component (a) has an average C / N ratio greater than or equal to 6.5, in particular greater than or equal to 7.5, in particular greater than or equal to 8.5, more particularly greater than or equal to 9.5 and in particular greater than or equal to 10 and preferably greater than or equal to 11. Preferably, the polyamide component (a) has an average number molecular weight Mn ranging from 10000 g / mol to 85000 g / mol, in particular from 10000 g / mol to 60000 g / mol, in particular from 10000 g / mol to 50000 g / mol, even more preferably from 12000 g / mol to 50000 g / mol.

[0090] These Mn values ​​may correspond to an inherent viscosity greater than or equal to 0.8 dL / g, as determined in m-cresol according to ISO 307:2007 but by changing the solvent (using m-cresol instead of sulfuric acid and the temperature being 20°C).

[0091] To minimize the risk of a reaction, it is also preferred that the polyamide component (a) contain less than 1000 ppm of a polycondensation catalyst, particularly one based on phosphorus. In particular, the catalyst content in the polyamide component (a) may be less than 500 ppm, preferably less than 100 ppm. According to one embodiment, the content of the polycondensation catalyst, particularly one based on phosphorus, in the polyamide component (a) is in the range of more than 0 ppm to 100 ppm, preferably more than 0 ppm to less than 90 ppm, preferably more than 0 ppm to 80 ppm, preferably more than 0 ppm to 70 ppm, preferably more than 0 ppm to 60 ppm, preferably more than 0 ppm to 50 ppm.

[0092] The nature of the catalyst can be determined, in particular, by GC-MS spectroscopy. In the case of a catalyst containing protons, such as phosphorus catalysts, the phosphorus content and its nature can be determined by phosphorus nuclear magnetic resonance spectroscopy (P31 NMR), for example, on an AVANCE 400 NEO spectrometer. Samples are solubilized at room temperature in a HFIP / CD2Cl2 mixture (in a 3:1 v / v ratio). The sample size is approximately 500 mg. The analysis is performed using the method without an internal standard. From the phosphorus NMR spectrum, the mass content of H3PO2 can be determined relative to the composition. Alternatively, the phosphorus content can also be determined by techniques known to those skilled in the art, such as elemental analysis or atomic spectroscopy.

[0093] Preferably, the polyamide component (a) also comprises at least 50% by weight, preferably at least 70% by weight, and particularly at least 90% by weight, or even 100% by weight, of polyamide having non-reactive end-chain functionalities. The term "non-reactive end-chain functionalities" means functionalities that do not react with a carboxylic acid or a primary amine in reactive extrusion. These functionalities may be selected, in particular, from alkyl and alcohol functionalities; preferably, they are alkyl functionalities.

[0094] Finally, the polyamide component (a) preferably has a ratio between the end-chain amine and carboxylic acid (NH2 / COOH) functions greater than 1, and preferably greater than 1.01.

[0095] The concentration of NH2 groups at the ends of the chain can be measured using a potentiometric titration. This titration can be performed, for example, as follows: the polyamides are first dissolved in m-cresol at 80°C, and then the terminal NH2 groups are titrated with a perchloric acid solution. The concentration of COOH groups at the ends of the chain can be determined by potentiometric analysis. A measurement protocol is detailed in the article "Synthesis and characterization of poly(copolyethers-block-polyamides) - Characterization and properties of the multiblock copolymers," Maréchal et al., Polymer, Volume 41, 2000, 3561-3580. The (NH2 / COOH) ratio is then obtained by dividing the two concentrations.

[0096] Preferably, polyamide A consists of a single homopolyamide. Even more preferably, polyamide B also consists of a single homopolyamide. More advantageously, polyamides A and B consist of an aliphatic semi-crystalline homopolyamide. More advantageously, polyamides A and B consist of an aliphatic semi-crystalline homopolyamide, the aliphatic semi-crystalline homopolyamide B being different from the aliphatic semi-crystalline homopolyamide A.

[0097] Preferably, polyamide B differs from polyamide A in its average molecular weight in number (Mn). In particular, polymer B may have a number (Mn) that differs from that of polyamide A by more than 3%, advantageously by more than 5%, and especially by more than 10%. Polyamide B may also differ from polyamide A in its dispersity. In particular, polymer B may have a dispersity that differs from that of polyamide A by more than 3%, advantageously by more than 5%, and especially by more than 10%.

[0098] Polyamide B can also differ from polyamide A in the content of end-chain functional groups. These functional groups can include amine or carboxylic acid groups. In particular, polymer B can have a different content of amine and / or carboxylic acid end-chain functional groups than polyamide A by more than 3%, advantageously more than 5%, and especially more than 10%.

[0099] Polyamide B can also differ from polyamide A in its average C / N ratio. In particular, polymer B can have an average C / N ratio that differs from that of polyamide A by more than 1, advantageously greater than 1.5, and especially greater than 2.

[0100] In one embodiment, polyamide B differs from polyamide A in molar mass, dispersity and C / N ratio by at least 1, for example the difference between the molar mass of polyamide A and that of polyamide B is greater than 3%, advantageously greater than 5% and the difference between the dispersity of polyamide A and that of polyamide B is greater than 3%, advantageously greater than 5%, and the difference between the C / N ratio of polyamide A and that of polyamide B is greater than 1.

[0101] In one embodiment, polyamide B differs from polyamide A in molar mass, dispersity, chain ends and C / N ratio, for example the difference between the molar mass of polyamide A and that of polyamide B is greater than 3%, advantageously greater than 5% and the difference between the dispersity of polyamide A and that of polyamide B is greater than 3%, advantageously greater than 5%, the chain ends of polyamides A and B are different and the difference between the C / N ratio of polyamide A and that of polyamide B is greater than 1.

[0102] Advantageously, the polyamide component (a) consists of polyamides whose inherent viscosity difference, between the polyamide with the lowest inherent viscosity and the one with the highest inherent viscosity, is greater than 0.1 dL / g, in particular greater than 0.2 dL / g, and especially greater than 0.4 dL / g. Preferably, the polyamide composition of the invention has an inherent viscosity of less than 1.7 dL / g, in particular less than 1.5 dL / g, and especially less than 1.3 dL / g. According to one embodiment, the composition has an inherent viscosity between 0.9 dL / g and 1.7 dL / g, for example between 1.0 dL / g and 1.3 dL / g. The inherent viscosity is determined in m-cresol according to ISO 307:2007 but by changing the solvent (using m-cresol instead of sulfuric acid and the temperature being 20°C).

[0103] Preferably, the polyamide component (a) comprises at least 30%, in particular at least 40%, in particular at least 50%, in particular at least 60%, more particularly at least 70%, even more particularly at least 80%, and especially 90% by weight of recycled polyamide. Particularly advantageously, the polyamide component (a) of the composition consists of 100% recycled polyamide.

[0104] Preferably, the recycled polyamide in the composition is characterized by the presence of functional groups resulting from oxidation reactions selected from primary amides, nitriles, methyl end groups, alkenes, formamides, imides, carboxylic acids, alcohols, and mixtures thereof, in a molar ratio relative to amides greater than that of the same polyamide in a new, unused article. These functional groups resulting from oxidation reactions may be present in the recycled polyamide in a molar ratio relative to secondary amides greater than 10%, for example, greater than 100%, greater than 150%, or greater than 300%, compared to that of the same virgin polyamide.

[0105] During the use of a manufactured object, new species resulting from oxidation mechanisms, including primary amide, nitrile, methyl end-chain, alkene, formamide, imide, carboxylic acid, and alcohol functional groups, may appear in the polyamides constituting said object. These functional groups appear due to UV radiation, heat, or a reaction with a compound with which the object comes into contact, for example, gasoline, sunscreen, lubricants, etc.

[0106] These functional groups can be detected by infrared spectrometry or NMR. Concentrations can be measured by proton NMR in dichloromethane-d2, after adding HFIP (hexafluoroisopropanol) to solubilize the polyamide. For example, 20 mg of polymer can be dissolved in 0.7 mL of solvent with a H₂FlP / CD₂Cl ratio of 1 / 3.

[0107] Some of the functions mentioned above can be observed in NMR of13 C. Thus, the 36 ppm line corresponds to the CH2 α-membered group of the primary amide, and the 34 ppm line corresponds to the CH2 α-membered group of the carboxylic acid. These species can be quantified by integrating the area under the lines and comparing it to the area under the 37.1 ppm line corresponding to the secondary amide. Similarly, the lines corresponding to the carbonyl groups of the primary amide, carboxylic acid, and secondary amide functions are observed at 181.2 ppm, 179.6 ppm, and 177.4 ppm, respectively. The 16.7 ppm line corresponds to the CH2 α-membered group of the nitrile group. The formamide group exhibits chemical shifts at 163.0 ppm and 166.3 ppm.

[0108] Other functions mentioned above can be observed by proton NMR (¹H NMR) in the solvent H₂Fl₂P / CD₂Cl₂ as described above. The C₆H₁₂O lines of formamides are observed at 7.92 and 8.01 ppm. The line corresponding to the CH₂enα lines of primary amides can be observed at 2.30 ppm. The 0.9 ppm line corresponds to the CH₃ groups of the type CH₃-(CH₂). n The line at 2.40 ppm corresponds to the CH2 at the α position of the nitrile function. Similar to what is described for carbon NMR, the ratios of new functions relative to secondary amides can be determined by integrating the area under the lines and comparing them to the area under the line corresponding to the CH2 at the α position of the secondary amide (2.20 ppm).

[0109] Furthermore, in infrared spectroscopy, the absorption band is from 1700 to 1740 cm⁻¹ 1 corresponds to an imide, that of 1680 to 1720 cm 1 to the carbonyl of the carboxylic acid and that of 3580 to 3670 cm 1corresponds to the alcohol function of the carboxylic acid. The absorption band is from 3580 to 3670 cm⁻¹. 1 corresponds to the free alcohol function. The amide function is characterized, on the one hand, by a pair of absorption bands from 3100 to 3500 cm⁻¹ 1 and from 1560 to 1640 cm 1 which corresponds to the NH group of the amide and, on the other hand, by the absorption band from 1650 to 1700 cm 1 which corresponds to the carbonyl group of the amide.

[0110] The molar ratio of functions resulting from oxidation reactions relative to secondary amide functions can range from 0.0001 to 0.3.

[0111] The molar ratio of imide functions to secondary amide functions can be from 0.0005 to 0.02, in particular from 0.001 to 0.08, especially from 0.005 to 0.05.

[0112] The molar ratio of carboxylic acid functions to secondary amide functions is preferably between 0.0005 and 0.02, in particular between 0.001 and 0.08, especially between 0.005 and 0.05.

[0113] Preferably, the molar ratio of alcohol functions to secondary amide functions is from 0.0005 to 0.02, in particular from 0.001 to 0.08, in particular from 0.005 to 0.05.

[0114] Moreover, the said molar ratio of primary amide functions to secondary amide functions is preferably between 0.0005 and 0.1, in particular between 0.001 and 0.08, in particular between 0.005 and 0.05.

[0115] Said molar ratio of nitrile functions to secondary amide functions is preferably between 0.0005 and 0.1, in particular between 0.001 and 0.08, in particular between 0.005 and 0.05.

[0116] The molar ratio of alkene functions to secondary amide functions can be from 0.0005 to 0.1, in particular from 0.001 to 0.08, especially from 0.005 to 0.05.

[0117] The molar ratio of formamide functions to secondary amide functions can be from 0.0005 to 0.1, in particular from 0.001 to 0.08, especially from 0.005 to 0.05.

[0118] Finally, the molar ratio of methyl functions at the end of the chain relative to secondary amide functions is preferably between 0.0005 and 0.2, in particular between 0.001 and 0.08, in particular between 0.005 and 0.05.

[0119] Charges (b)

[0120] The composition of the invention may comprise from 0 to 65%, preferably more than 0 to 65%, in particular 5% to 60%, in particular 10% to 50%, in particular 20% to 40% and in particular 25% to 30% by weight of fillers.

[0121] The fillers can be chosen from among: - Reinforcing fibers;

[0122] - Conductive fillers such as carbon black and carbon nanotubes;

[0123] - Flame retardant agents (HFFR);

[0124] - Fillers that reduce the density of the composition, such as hollow glass beads;

[0125] - Heat-conducting fillers, notably chosen from metal oxides such as alumina (Al2O3), aluminosilicate (Al2SiO5) and ceramics such as boron nitride (BN) and aluminium nitride (AIN).

[0126] Reinforcing fibers are particularly preferred fillers. They can be of mineral, organic, or plant origin. Reinforcing fibers can also be coated or uncoated. Therefore, reinforcing fibers can be coated with up to 0.1% by weight of an organic material (such as a thermosetting or thermoplastic resin) forming the coating.

[0127] Among the mineral-based fibers, we can mention carbon fibers, glass fibers, basalt or basalt-based fibers, silica fibers, and silicon carbide fibers.

[0128] Examples of organic fibers include thermoplastic or thermosetting polymer fibers, such as semi-aromatic polyamide fibers, aramid fibers, and polyolefin fibers. In one embodiment, organic fibers do not include semi-aromatic polyamide fibers. In another embodiment, organic fibers are selected from thermoplastic or thermosetting polymer fibers, such as semi-aromatic polyamide fibers and aramid fibers. In yet another embodiment, organic fibers are selected from thermoplastic or thermosetting polymer fibers, such as semi-aromatic polyamide fibers and aramid fibers, but exclude semi-aromatic polyamide fibers.

[0129] Among plant-based fibers, we can mention natural fibers made from flax, hemp, lignin, bamboo, silk (particularly spider silk), sisal, and other cellulosic fibers, especially viscose. These plant-based fibers can be used pure, treated, or coated with a layer to facilitate adhesion and impregnation of the thermoplastic polymer matrix.

[0130] Preferably, the reinforcing fiber is chosen from glass fibers, carbon fibers, basalt fibers and basalt-based fibers, especially from carbon fibers and glass fibers and especially glass fibers.

[0131] Glass fibers can have a circular or non-circular cross-section. Examples of non-circular fibers include elliptical, oval, cocoon, star, flake, flat, cruciform, polygonal, or annular cross-sections. Advantageously, glass fibers have a circular cross-section. Glass fibers are notably of type E, R, S2, or T. Advantageously, type E glass fibers are used. In a preferred embodiment, the fillers are recycled. For fillers containing glass, they can be manufactured from industrial production waste or post-consumer recycled glass. Carbon fibers, for example, can be obtained from the cutting of spools of long, expired fibers, particularly carbon fibers used in the aerospace industry.

[0132] Advantageously, the fillers are chosen from glass fibers, especially circular section fibers, and carbon fibers, especially glass fibers, especially circular section fibers.

[0133] Shock modifier (c)

[0134] The polyamide composition of the invention further comprises 0 to 30%, 0 to 20%, and in particular 0 to 10% by weight of at least one impact modifier. According to one embodiment, the polyamide composition of the invention comprises more than 0 to 30%, preferably more than 0 to 20%, and preferably more than 0 to 10% by weight of at least one impact modifier.

[0135] The shock modifier is advantageously a polymer with a flexural modulus of less than 100 MPa (measured according to ISO 178:2010, at 23°C with a relative humidity of RH50%), and a Tg of less than 0°C (measured according to standard 11357-2:2013 at the inflection point of the DSC thermogram, at a heating rate of 20K / min).

[0136] In particular, it may be a polyolefin, or a PEBA, especially a PEBA with a flexible PTMG segment.

[0137] The polyolefin can be functionalized or non-functionalized or be a mixture of at least one functionalized polyolefin and / or at least one non-functionalized polyolefin.

[0138] An unfunctionalized polyolefin can typically be a homopolymer or copolymer of alpha olefins or diolefins, such as ethylene, propylene, 1-butene, 1-octene, or butadiene. Examples include:

[0139] - homopolymers and copolymers of polyethylene, in particular LDPE, HDPE, LLDPE (linear low density polyethylene), VLDPE (very low density polyethylene) and metallocene polyethylene;

[0140] - homopolymers or copolymers of propylene;

[0141] - ethylene / alpha-olefin copolymers such as ethylene / propylene, EPR (short for ethylene-propylene-rubber) and ethylene / propylene / diene (EPDM);

[0142] - the block copolymers styrene / ethylene-butene / styrene (SEBS), styrene / butadiene / styrene (SBS), styrene / isoprene / styrene (SIS), styrene / ethylene-propylene / styrene (SEPS); and

[0143] - copolymers of ethylene with at least one product selected from the salts or esters of unsaturated carboxylic acids such as alkyl (meth)acrylate (e.g. methyl acrylate), or vinyl esters of saturated carboxylic acids such as vinyl acetate (EVA), the proportion of comonomer up to 40% by weight.

[0144] Functionalized polyolefins can be, in particular, alpha-olefin polymers with reactive motifs (functionalities); such reactive motifs are acid, anhydride, or epoxy groups. Examples include the aforementioned polyolefins grafted or co- or ter-polymerized with unsaturated epoxides such as glycidyl (meth)acrylate, or with carboxylic acids or their corresponding salts or esters such as (meth)acrylic acid (which can be totally or partially neutralized by metals such as Zn, etc.) or with carboxylic acid anhydrides such as maleic anhydride. A functionalized polyolefin is for example a PE / EPR mixture, the weight ratio of which can vary widely, for example between 40 / 60 and 90 / 10, said mixture being co-grafted with an anhydride, in particular maleic anhydride, according to a grafting rate for example of 0.01% to 5% by weight.

[0145] The functionalized polyolefin can be chosen from the following (co)polymers, grafted with maleic anhydride or glycidyl methacrylate, in which the grafting rate is, for example, from 0.01% to 5% by weight:

[0146] - PE, PP, copolymers of ethylene with propylene, butene, hexene, or octene containing, for example, 35% to 80% by weight of ethylene;

[0147] - ethylene / alpha-olefin copolymers such as ethylene / propylene, EPR (short for ethylene-propylene-rubber) and ethylene / propylene / diene (EPDM);

[0148] - the block copolymers styrene / ethylene-butene / styrene (SEBS), styrene / butadiene / styrene (SBS), styrene / isoprene / styrene (SIS), styrene / ethylene-propylene / styrene (SEPS);

[0149] - ethylene and vinyl acetate (EVA) copolymers, containing up to 40% by weight of vinyl acetate;

[0150] - ethylene and alkyl (meth)acrylate copolymers, containing up to 40% by weight of alkyl (meth)acrylate; and

[0151] - ethylene and vinyl acetate (EVA) and alkyl (meth)acrylate copolymers, containing up to 40% by weight of comonomers.

[0152] The functionalized polyolefin can also be selected from ethylene / propylene copolymers major in propylene grafted with maleic anhydride and then condensed with mono-amino polyamide (or a polyamide oligomer) (products described in EP-A-0342066).

[0153] Functionalized polyolefins can also be co- or terpolymers of at least the following repeating units: (1) ethylene, (2) alkyl (meth)acrylate or saturated vinyl ester of carboxylic acid, and (3) anhydrides such as maleic anhydride or (meth)acrylic acid, or epoxies such as glycidyl (meth)acrylate. Examples of functionalized polyolefins of this latter type include the following copolymers, where ethylene preferably represents at least 60% by weight and the ter monomer (the functional group) represents, for example, 0.1% to 10% by weight of the copolymer:

[0154] - ethylene / alkyl (meth)acrylate / (meth)acrylic acid or maleic anhydride or glycidyl methacrylate copolymers;

[0155] - ethylene / vinyl acetate / maleic anhydride or glycidyl methacrylate copolymers;

[0156] - ethylene / vinyl acetate copolymers or alkyl (meth)acrylate / (meth)acrylic acid or maleic anhydride or glycidyl methacrylate.

[0157] In the preceding copolymers, (meth)acrylic acid can be salified with Zn or Li.

[0158] The term "alkyl (meth)acrylate" in functionalized or non-functionalized polyolefins refers to methyl acrylates and alkyl acrylates in C1 to C1g, and may be selected from methyl acrylate, ethyl acrylate, n-butyl acrylate, isobutyl acrylate, ethyl-2-hexyl acrylate, cyclohexyl acrylate, methyl methacrylate and ethyl methacrylate.

[0159] Furthermore, the aforementioned polyolefins can also be crosslinked by any suitable process or agent (diepoxy, diacid, peroxide, etc.); the term functionalized polyolefin also includes mixtures of the aforementioned polyolefins with a difunctional reagent such as diacid, dianhydride, diepoxy, etc. capable of reacting with them or mixtures of at least two functionalized polyolefins capable of reacting with each other.

[0160] The copolymers mentioned above can be copolymerized statistically or sequentially and exhibit a linear or branched structure.

[0161] The molecular weight, MFI, and density of these polyolefins can also vary considerably, a fact that those skilled in the art will appreciate. MFI, short for Melt Flow Index, is the index of fluidity in the melt state. It is measured according to the ASTM 1238 standard.

[0162] Advantageously, non-functionalized polyolefins are selected from homopolymers or copolymers of polypropylene and any homopolymer of ethylene or copolymer of ethylene and a higher alpha-olefin comonomer such as butene, hexene, octene, or 4-methyl-1-pentene. Examples include PP, high-density polyethylene (HDPE), medium-density polyethylene (MDPE), linear low-density polyethylene (LLDPE), low-density polyethylene (LDPE), and ultra-low-density polyethylene (ULPE). These polyethylenes are known to those skilled in the art to be produced by a "radical" process, by Ziegler-type catalysis, or, more recently, by so-called "metallocene" catalysis.

[0163] Advantageously, functionalized polyolefins are selected from any polymer comprising alpha-olefin motifs and motifs bearing polar reactive functions such as epoxy, carboxylic acid, or carboxylic acid anhydride groups. Examples of such polymers include terpolymers of ethylene, alkyl acrylate, and maleic anhydride or glycidyl methacrylate, such as SKFP's Lotader®, or polyolefins grafted with maleic anhydride, such as SKFP's Orevac®, as well as terpolymers of ethylene, alkyl acrylate, and (meth)acrylic acid. Also included are homopolymers or copolymers of polypropylene grafted with a carboxylic acid anhydride and then condensed with polyamides or monoamino polyamide oligomers.

[0164] Plasticizer (d)

[0165] The polyamide composition of the invention also comprises 0 to 15%, in particular 0 to 5%, especially 0 to 1.5%, of at least one plasticizer. According to one embodiment, the polyamide composition comprises more than 0 to 15%, in particular more than 0 to 5%, preferably more than 0 to 1.5%, of at least one plasticizer.

[0166] The plasticizer can in principle be any plasticizer from among those commonly used in polyamide-based compositions.

[0167] Advantageously, a plasticizer is used which has good thermal stability so that no fumes are formed during the mixing stages of the different polymers and the transformation of the resulting composition.

[0168] In particular, this plasticizer can be chosen from: benzene sulfonamide derivatives such as n-butyl benzene sulfonamide (BBSA), the ortho and para isomers of ethyl toluene sulfonamide (ETSA), N-cyclohexyl toluene sulfonamide and N-(2-hydroxypropyl) benzene sulfonamide (HP-BSA), esters of hydroxybenzoic acids such as ethyl-2-hexyl para-hydroxybenzoate (EHPB) and decyl-2-hexyl para-hydroxybenzoate (HDPB), esters or ethers of tetrahydrofurfuryl alcohol such as oligoethyleneoxy-tetrahydrofurfuryl alcohol, and esters of citric acid or hydroxymalonic acid, such as oligoethyleneoxymalonate.

[0169] A preferred plasticizer is n-butyl benzene sulfonamide (BBSA).

[0170] Another particularly preferred plasticizer is N-(2-hydroxy-propyl)benzenesulfonamide (HP-BSA). This has the advantage of preventing the formation of deposits on the screw and / or extrusion die ("die tears") during an extrusion processing step.

[0171] A mixture of plasticizers can obviously be used.

[0172] Preferably, the polyamide composition is free of plasticizers.

[0173] Additives (e)

[0174] The polyamide composition also includes 0 to 5%, preferably more than 0 to 5%, in particular 0.1% to 5%, notably 0.1% to 2% by weight of at least one additive. This at least one additive may be selected from among basic reagents, stabilizers, colorants, processing aids, surfactants, nucleating agents, pigments, brighteners, antioxidants, lubricants, waxes, flame retardants, or a mixture thereof.

[0175] As an example, the stabilizer may be a UV stabilizer, an organic stabilizer or more generally a combination of organic stabilizers, such as a phenol-type antioxidant (for example Irganox® 245 or 1098 or 1010 from Ciba-BASF), a phosphite-type antioxidant (for example Irgafos® 126 or Irgafos® 168 from Ciba-BASF), a HALS (Hindered Amine Light Stabiliser or hindered amine light stabilizer for example Tinuvin® 770 from Ciba-BASF), an anti-UV (for example Tinuvin® 312 from Ciba) or a phosphorus-based stabilizer. One can also use amine-type antioxidants such as Naugard® 445 from Crompton or polyfunctional stabilizers such as Nylostab® S-EED from Clariant.

[0176] This stabilizer can also be a mineral stabilizer, such as a copper-based stabilizer. Examples of such mineral stabilizers include copper halides and copper acetates. Other metals, such as silver, could also be considered, but these are known to be less effective. These copper-based compounds are typically associated with alkali metal halides, particularly potassium.

[0177] In particular, the composition may include, as an additive (e), one or more basic compounds. Preferably, the basic reagent has a pKa greater than 7, advantageously 8, and preferably 9.

[0178] Advantageously, the basic reagent is chosen from stearates, carbonates, and hydroxides. Preferably, the basic reagent contains a cation chosen from Ca²⁺, Na⁺, K⁺, Mg²⁺, and Cu⁺. The preferred basic reagents are potassium hydroxide and sodium hydroxide.

[0179] The basic reagent is capable of reacting with carboxylic acid functions to form groups with the following formula:

[0180] COO- X+ in which

[0181] X+ designates a cation, particularly a metallic cation, specifically chosen from Ca++, Na+, K+, Mg++, and Cu+. When X+ designates a dibasic cation, particularly a metallic cation, specifically chosen from Ca++ or Mg++, X+ associates with 2 COO- ions. When X+ designates a monobasic cation, particularly a metallic cation, specifically chosen from Na+ or Cu+, X+ associates with 1 COQ- ion.

[0182] Useful synergistic flame retardant agents are described in particular in WQ2005121234.

[0183] They can be chosen from nitrogen synergists and phosphorus / nitrogen synergists. Nitrogen synergists preferably include benzoguanamine, tris(hydroxyethyl)isocyanurate, allantoin, glycolurile, melamine, melamine cyanurate, dicyandiamide, guanidine, and carbodiimides.

[0184] Nitrogen synergists preferably comprise melamine condensation products. For example, melamine condensation products include melem, melam, or melon, or compounds of this type with a higher degree of condensation, or a mixture thereof, and, for example, may be prepared by the process described in US patent 5,985,960.

[0185] Phosphorus / nitrogen synergists may include reaction products of melamine with phosphoric acid or with condensed phosphoric acids, or include reaction products of condensation products of melamine with phosphoric acid or condensed phosphoric acids, or include a mixture of the specified products.

[0186] In one embodiment, the additives are chosen from antioxidants, colour pigments and flame retardant synergists, in particular nitrogen synergists, especially melamine-based.

[0187] According to another aspect, the present invention relates to the use of a composition as defined above for the manufacture of an article by injection, in particular a sporting article, an article of interest in the field of industry, electronics or optics.

[0188] In yet another aspect, the present invention relates to a method for preparing a composition as defined above, comprising the step of (i) mixing the constituents (a) - (e) in the molten state. Preferably, this step (i), also called the compounding step, is carried out in an extruder. Advantageously, it is conducted with a residence time in the extruder of less than five minutes. In one embodiment, the compounding step (i) is carried out in a twin-screw extruder, preferably the Coperion ZSK 26 MC twin-screw extruder. In one embodiment, the compounding step (i) is carried out at a machine temperature ranging from 100°C to 300°C, preferably from 200°C to 300°C, and more preferably at 270°C. According to one embodiment, the compounding step (i) is carried out with an extruder whose screw speed is fixed in a range of 200 to 300 rpm, preferably at 250 rpm.According to one embodiment, the compounding step (i) is carried out with an extruder whose output rate is fixed in the range of 10 to 30 kg / h, preferably 15 to 25 kg / h, preferably 20 kg / h. According to another embodiment, the compounding step (i) is carried out with a residence time in the extruder ranging from 0 to 5 minutes. According to another embodiment, the composition of the invention at the end of the compounding step (i) is in the form of granules. In yet another aspect, the present invention relates to a method for producing a composition as defined above, characterized in that it comprises an extrusion or injection step of said composition at a temperature below 300°C, preferably 260°C, in particular with a residence time of less than 5 minutes.According to one embodiment, the extrusion or injection step of said composition of the invention is carried out at a temperature ranging from 240°C to less than 300°C.

[0189] EXAMPLES

[0190] The polyamide compositions in the examples below were prepared by standard compounding according to the following protocol.

[0191] Compounding for the preparation of granules of compositions

[0192] Coperion ZSK 26 MC twin-screw extruder with at least one lateral feed channel for raw materials

[0193] Machine temperature: 270°C

[0194] Screw speed: 250 rpm

[0195] Extruder output: 20 kg / h

[0196] Transformation

[0197] To evaluate the mechanical properties, the granules obtained above were transformed into 80mm x 10mm x 4mm test specimens by injection molding. The following parameters were used:

[0198] - ENGEL VICTORY 500 hydraulic press, 160T

[0199] - Injection temperature (feed / nozzle): 240 / 260 °C for Ell, E 12 and EC1 and 280 / 300 °C for EC2

[0200] - Mold temperature: 50°C

[0201] Impact resistance was determined according to ISO 179-1: 2010 (Charpy impact) on notched 80mm x 10mm x 4mm specimens, at a temperature of -30°C + / -2°C on dry samples.

[0202] Dispersion measurement

[0203] Dispersion was determined as the ratio of the weight-average molecular mass (Mw) to the number-average molecular mass (Mn). The number-average molecular mass (Mn) and weight-average molecular mass (Mw) were measured by gel permeation chromatography according to the following protocol, based on ISO 16014-1:2012. The polyamide was solubilized at a concentration of 2 g / L in hexafluoroisopropanol stabilized with 0.05 M potassium trifluoroacetate for 24 h at room temperature (20°C).The resulting solution is then filtered through a PTFE membrane with a porosity of 0.2 pm, and then injected at a flow rate of 1 mL / min into a liquid chromatography system equipped with a set of PFG columns from Polymer Standards Service consisting of a pre-column measuring 50 x 8 mm, a 1000 Å column measuring 300 x 8 mm with a particle size of 7 pm, and a 100 Å column measuring 300 x 8 mm with a particle size of 7 pm. Molar masses are measured by the refractive index and are expressed in PMMA equivalents, used as a calibration standard, and then converted to g / mol.

[0204] The results are presented in Table 1 below.

[0205] [Table 1]: Composition of the formulations studied

[0206] *The inherent viscosity is determined in m-cresol according to ISO 307:2007, but with a change of solvent (using m-cresol instead of sulfuric acid) and a temperature of 20°C. **The EI2 recycled product blend can comprise from 2 to 15 different grades of polyamide 11 (PA11), provided that the inherent viscosity of the blend is 0.95 dL / g and the dispersity of the blend is 2.5. The compositions according to the invention exhibit improved cold shock properties. EC2 shows that a semi-aromatic polyamide, although exhibiting high dispersity, has poorer shock properties.

Claims

DEMANDS 1. Polyamide composition comprising, by weight: (a) 35% to 100% of a polyamide component comprising, by weight relative to the total weight of the polyamide component: a. 50% to 95% of at least one polyamide A, b. 5% to 50% of at least one polyamide B other than polyamide A, (b) from 0 to 65% of charges, (c) 0 to 30% of at least one shock modifier, (d) 0 to 15% of at least one plasticizer, and (e) of 0 to 5% of at least one additive, the sum of constituents (a) to (e) being equal to 100%, wherein: the polyamide component (a) of the composition has a dispersity (D) greater than 2.25, in particular greater than 2.35, in particular from 2.5 to 15, preferably from 2.5 to 10, more preferably from 2.5 to 5; said dispersity (D) being measured by gel permeation chromatography according to ISO 16014-1:2012.

2. Composition of polyamides according to claim 1, wherein the polyamide component (a) comprises at least 50%, advantageously 75%, preferably 95%, in particular 100% aliphatic polyamide.

3. Composition of polyamides according to claim 1 or 2, wherein the polyamide component (a) has a C / N ratio greater than or equal to 6.5, in particular greater than or equal to 7.5, in particular greater than or equal to 8.5, more particularly greater than or equal to 9.

5.

4. Polyamide composition according to any one of claims 1 to 3, wherein the polyamide component (a) comprises less than 1000 ppm of catalyst and / or polyamides having non-reactive end-chain functions and / or polyamides having an NH2 / COOH end-chain function ratio greater than 1.

5. Composition of polyamides according to any one of claims 1 to 4, wherein the inherent viscosity difference between polyamide A and B is greater than 0.1 dL / g, in particular greater than 0.2 dL / g, in particular greater than 0.4 dL / g.

6. Composition of polyamides according to any one of claims 1 to 5, having an inherent viscosity of less than 1.7 dL / g, in particular less than 1.5 dL / g, in particular less than 1.3 dL / g, said inherent viscosity being determined in m-cresol according to ISO 307:2007 but changing the solvent (using m-cresol instead of sulfuric acid and the temperature being 20°C).

7. Polyamide composition according to any one of claims 1 to 6, wherein the polyamide component (a) comprises at least 30% recycled polyamide, said recycled polyamide being a polyamide having one or more functions resulting from oxidation reactions selected from the primary amide, nitrile, methyl group at the end of the chain, alkene, formamide, imide, carboxylic acid and alcohol functions, in a molar ratio with respect to the amide functions greater than that of the same polyamide constituting an unused article which has never been used.

8. Composition according to claim 7, wherein the molar ratio of functions resulting from oxidation reactions relative to secondary amide functions is from 0.0001 to 0.

3.

9. Composition according to claim 7 or 8, wherein the molar ratio of imide functions to secondary amide functions is from 0.0005 to 0.02, in particular from 0.001 to 0.08, in particular from 0.005 to 0.

05.

10. Composition according to any one of claims 7 to 9, wherein the molar ratio of carboxylic acid functions to secondary amide functions is from 0.0005 to 0.02, in particular from 0.001 to 0.08, in particular from 0.005 to 0.

05.

11. Composition according to any one of claims 7 to 10, wherein the molar ratio of alcohol functions to secondary amide functions is from 0.0005 to 0.02, in particular from 0.001 to 0.08, in particular from 0.005 to 0.

05.

12. Composition according to any one of claims 7 to 11, wherein the molar ratio of nitrile functions to secondary amide functions is from 0.0005 to 0.02, in particular from 0.001 to 0.08, in particular from 0.005 to 0.

05.

13. Use of a composition according to any one of claims 1 to 12 for the manufacture of an article by injection.

14. A method for preparing a composition according to any one of claims 1 to 12, comprising the step of: (i) mix the components (a) to (e) in a molten state, in particular in an extruder.

15. Preparation method according to claim 14, wherein step (i) is carried out with a residence time of less than five minutes.

16. Method of implementing a composition according to any one of claims 1 to 12, comprising an extrusion or injection step of said composition at a temperature below 300 °C, preferably within a range from 200 °C to less than 300 °C, preferably 280 °C.

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