Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
  • C08J9/0061—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof characterized by the use of several polymeric components
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
  • B29C44/34—Auxiliary operations
  • B29C44/3403—Foaming under special conditions, e.g. in sub-atmospheric pressure, in or on a liquid
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/30—Low-molecular-weight compounds
  • C08G18/32—Polyhydroxy compounds; Polyamines; Hydroxyamines
  • C08G18/3203—Polyhydroxy compounds
  • C08G18/3206—Polyhydroxy compounds aliphatic
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/40—High-molecular-weight compounds
  • C08G18/48—Polyethers
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  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/65—Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
  • C08G18/66—Compounds of groups C08G18/42, C08G18/48, or C08G18/52
  • C08G18/6603—Compounds of groups C08G18/42, C08G18/48, or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38
  • C08G18/6607—Compounds of groups C08G18/42, C08G18/48, or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/3203
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
  • C08G18/72—Polyisocyanates or polyisothiocyanates
  • C08G18/73—Polyisocyanates or polyisothiocyanates acyclic
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
  • C08G18/72—Polyisocyanates or polyisothiocyanates
  • C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
  • C08G18/76—Polyisocyanates or polyisothiocyanates cyclic aromatic
  • C08G18/7657—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings
  • C08G18/7664—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups
  • C08G18/7671—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups containing only one alkylene bisphenyl group
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
  • C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
  • C08J9/12—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L75/00—Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
  • C08L75/04—Polyurethanes
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L75/00—Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
  • C08L75/04—Polyurethanes
  • C08L75/08—Polyurethanes from polyethers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L77/00—Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2201/00—Foams characterised by the foaming process
  • C08J2201/02—Foams characterised by the foaming process characterised by mechanical pre- or post-treatments
  • C08J2201/03—Extrusion of the foamable blend
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2375/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
  • C08J2375/04—Polyurethanes
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2375/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
  • C08J2375/04—Polyurethanes
  • C08J2375/08—Polyurethanes from polyethers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2377/00—Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2475/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
  • C08J2475/04—Polyurethanes
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2475/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
  • C08J2475/04—Polyurethanes
  • C08J2475/08—Polyurethanes from polyethers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2477/00—Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers

Definitions

• the present invention relates to polymer foams, comprising a thermoplastic polyurethane and a copolymer with polyamide blocks and amine chain-ended polyether blocks, as well as methods of preparing the same.
• Various polymer foams are used in particular in the field of sports equipment, such as soles or sole components, gloves, rackets or golf balls, individual protection elements in particular for the practice of sport (vests, interior parts of helmets , shells).
• Such applications require a set of particular physical properties ensuring ability to rebound, low permanent deformation in compression and an ability to withstand repeated impacts without deforming and returning to the initial shape.
• Document WO 2022/162048 relates to expanded particles comprising a first thermoplastic elastomer having a Shore D hardness of 20 to 90 and a second thermoplastic elastomer.
• the first thermoplastic elastomer is in particular a thermoplastic polyurethane, a thermoplastic polyetheramide, a thermoplastic copolyester, a polyetherester or a polyesterester
• the second thermoplastic elastomer is in particular a thermoplastic polyurethane, a thermoplastic polyetheramide, a polyetherester or a polyesterester or a styrene-copolymer thermoplastic butadiene.
• the invention firstly concerns a polymer foam comprising: - at least one thermoplastic polyurethane, and
• At least a portion of the total polyamide block and polyether block copolymer is covalently bonded to a thermoplastic polyurethane molecule via a urea function.
• the concentration of urea function is from 0.001 meq/g to 0.1 meq/g, more preferably from 0.003 meq/g to 0.08 meq /g, more preferably from 0.005 meq/g to 0.05 meq/g.
• the copolymer with polyamide blocks and polyether blocks has a concentration of NH2 amine function, as measured by potentiometric dosage in metacresol using a 0.02N perchloric acid solution, of 0.002 meq/g to 0.2 meq/g, preferably 0.005 to 0.1 meq/g.
• the quantity of polyamide blocks is at least 15% by weight, preferably at least 25% by weight, relative to the total weight of the foam.
• the copolymer with polyamide blocks and polyether blocks comprises at least 30% by weight, preferably at least 40% by weight, of polyamide blocks, relative to the total weight of the copolymer, as measured by NMR of the proton in a TFA/CDCI3 mixture (1/4 v/v).
• the at least one thermoplastic polyurethane is a copolymer with rigid blocks and soft blocks, the content of rigid blocks in the thermoplastic polyurethane, as measured by proton NMR in DMSO D6, being less than or equal to at 90% by weight, more preferably less than or equal to 80% by weight, more preferably from 30 to 60% by weight.
• the foam comprises, relative to the total weight of the foam:
• the at least one thermoplastic polyurethane is a copolymer with rigid blocks and soft blocks, in which:
• the flexible blocks are chosen from polyether blocks, polyester blocks, polycarbonate blocks and a combination of these, preferably the flexible blocks are chosen from polyether blocks, polyester blocks, and a combination of these, and are more preferably blocks of polytetrahydrofuran, polypropylene glycol and/or polyethylene glycol; and or
• the rigid blocks comprise units derived from 4,4'-diphenylmethane diisocyanate and/or 1,6-hexamethylene diisocyanate and, preferably, units derived from at least one chain extender chosen from 1,3-propanediol , 1,4-butanediol and/or 1,6-hexanediol.
• the polyamide blocks of the copolymer with polyamide blocks and polyether blocks comprising amine chain ends are blocks of polyamide 11, polyamide 12, polyamide 10, polyamide 6, polyamide 6.10, polyamide 6.12 , polyamide 6.13, polyamide 10.9, polyamide 10.10, polyamide 10.12 and/or polyamide 12.9, preferably polyamide 11, polyamide 12, polyamide 6, polyamide 6.12, polyamide 6.13, polyamide 10.9 and/ or polyamide 12.9; and/or the polyether blocks of the copolymer with polyamide blocks and polyether blocks comprising amine chain ends are blocks of polyethylene glycol and/or polypropylene glycol and/or polytetrahydrofuran.
• the foam has a density, as measured at 23°C according to the ISO 1183-1 standard, less than or equal to 800 kg/m 3 , preferably less than or equal to 400 kg/m 3 , more preferably less than or equal to 300 kg/m 3 , even more preferably less than or equal to 230 kg/m 3 .
• the foam has an Asker C hardness, as measured at 23°C according to standard ISO 7619-1, of 20 to 90, preferably of 25 to 70.
• the invention also relates to a method of manufacturing a foam as described above, comprising the following steps:
• a polymer composition comprising the at least one thermoplastic polyurethane and the at least one copolymer with polyamide blocks and polyether blocks comprising amine chain ends;
• the blowing agent is mixed with the polymer composition in the molten state, the foaming of the mixture being preferably carried out in a mold.
• the blowing agent is a physical blowing agent and is mixed with the polymer composition in the form of a solid preform, with foaming of the mixture preferably being carried out in an autoclave.
• the invention also relates to an article consisting of a foam as described above or comprising at least one element consisting of a foam as described above, preferably chosen from the soles of sports shoes, balls or balls, gloves, personal protective equipment, rail soles, automobile parts, construction parts and electrical and electronic equipment parts.
• the present invention makes it possible to meet the need expressed above. It more particularly provides a regular, homogeneous, low density polymer foam, having improved flexibility and good mechanical properties, in particular good tear resistance and good abrasion resistance, while maintaining high rebound resilience and a relatively low residual deformation in compression.
• thermoplastic polyurethane TPU
• NH 2 amine chain ends
• covalent bonds are formed between at least part of the copolymer with polyamide blocks and polyether blocks comprising amine chain ends and at least part of the thermoplastic polyurethane, and more particularly between the amine functions of the copolymer with polyamide blocks and polyether blocks and the urethane functions of the thermoplastic polyurethane or the isocyanate functions present in the precursors of the thermoplastic polyurethane.
• This reaction between at least part of the copolymer with polyamide blocks and polyether blocks comprising amine chain ends and at least part of the thermoplastic polyurethane allows better compatibility between these polymers.
• the quantities indicated for a given species may apply to that species according to all its definitions (as mentioned in this text), including more restricted definitions.
• the invention firstly relates to a foam comprising at least one copolymer with polyamide blocks and polyether blocks comprising amine chain ends and at least one thermoplastic polyurethane.
• the presence of amine chain ends in the copolymer with polyamide blocks and polyether blocks can be detected by a potentiometric assay according to the following method: a sample of material is dissolved in metacresol at 80°C, then the NH2 functions of this sample are measured potentiometrically using a 0.02N perchloric acid solution.
• PEBA Polyamide block and polyether block copolymer
• PEBAs result from the polycondensation of polyamide blocks (rigid or hard blocks) with reactive ends with polyether blocks (flexible or soft blocks) with reactive ends, in particular from the polycondensation of polyamide blocks with dicarboxylic chain ends with polyoxyalkylene blocks with ends of diamine chains, obtained for example by cyanoethylation and hydrogenation of aliphatic polyoxyalkylene a,oo-dihydroxylated blocks called polyetherdiols.
• Polyamide blocks with dicarboxylic chain ends come, for example, from the condensation of polyamide precursors in the presence of a chain-limiting dicarboxylic acid.
• Three types of polyamide blocks can advantageously be used.
• the polyamide blocks come from the condensation of a dicarboxylic acid, in particular those having from 4 to 36 carbon atoms, preferably those having from 4 to 20 carbon atoms, more preferably from 6 to 18 carbon atoms. carbon, and an aliphatic or aromatic diamine, in particular those having from 2 to 20 carbon atoms, preferably those having from 6 to 14 carbon atoms.
• a dicarboxylic acid in particular those having from 4 to 36 carbon atoms, preferably those having from 4 to 20 carbon atoms, more preferably from 6 to 18 carbon atoms. carbon
• an aliphatic or aromatic diamine in particular those having from 2 to 20 carbon atoms, preferably those having from 6 to 14 carbon atoms.
• dicarboxylic acids mention may be made of 1,4-cyclohexyldicarboxylic acid, butanedioic, adipic, azelaic, suberic, sebacic, dodecanedicarboxylic, octadecanedicarboxylic acids and terephthalic and isophthalic acids, but also dimerized fatty acids. .
• diamines examples include tetramethylene diamine, hexamethylenediamine, 1,10-decamethylenediamine, dodecamethylenediamine, trimethylhexamethylenediamine, isomers of bis-(4-aminocyclohexyl)-methane (BACM), bis -(3-methyl-4-aminocyclohexyl)methane (BMACM), and 2-2-bis-(3-methyl-4-aminocyclohexyl)-propane (BMACP), para-amino-di-cyclohexyl-methane ( PACM), isophoronediamine (IPDA), 2,6-bis-(aminomethyl)-norbornane (BAMN) and piperazine (Pip).
• BCM bis-(4-aminocyclohexyl)-methane
• BMACM bis -(3-methyl-4-aminocyclohexyl)methane
• polyamide blocks PA 4.12, PA 4.14, PA 4.18, PA 6.10, PA 6.12, PA 6.14, PA 6.18, PA 9.12, PA 10.10, PA 10.12, PA 10.14 and/or PA 10.18 are used.
• PA notation X.Y X represents the number of carbon atoms from diamine residues, and Y represents the number of carbon atoms from diacid residues, conventionally.
• the polyamide blocks result from the condensation of one or more a,oo-aminocarboxylic acids and/or one or more lactams having from 6 to 12 carbon atoms in the presence of a dicarboxylic acid having 4 with 18 carbon atoms or a diamine.
• lactams we can cite caprolactam, oenantholactam and lauryllactam.
• a,oo-amino carboxylic acid mention may be made of aminocaproic, amino-7-heptanoic, amino-10-decanoic, amino-11-undecanoic and amino-12-dodecanoic acids.
• the polyamide blocks of the second type are blocks of PA 10 (polydecanamide), PA 11 (polyundecanamide), PA 12 (polydodecanamide) or PA 6 (polycaprolactam).
• PA 10 polydecanamide
• PA 11 polyundecanamide
• PA 12 polydodecanamide
• PA 6 polycaprolactam
• PA X represents the number of carbon atoms from amino acid residues or lactam residues.
• the polyamide blocks result from the condensation of at least one a,oo-aminocarboxylic acid (or a lactam), at least one diamine and at least one dicarboxylic acid.
• polyamide PA blocks are prepared by polycondensation:
• said comonomer(s) ⁇ Z ⁇ being introduced in a weight proportion advantageously up to 50%, preferably up to 20%, even more advantageously up to 10% relative to all the polyamide precursor monomers;
• the dicarboxylic acid having Y carbon atoms is used as chain limiter, which is introduced in excess relative to the stoichiometry of the diamine(s).
• the polyamide blocks result from the condensation of at least two a,oo-aminocarboxylic acids or at least two lactams having from 6 to 12 carbon atoms or of a lactam and a aminocarboxylic acid not having the same number of carbon atoms in the possible presence of a chain limiter.
• aliphatic a,oo-aminocarboxylic acid mention may be made of aminocaproic, amino-7-heptanoic, amino-10-decanoic, amino-11-undecanoic and amino-12-dodecanoic acids.
• lactam we can cite caprolactam, oenantholactam and lauryllactam.
• aliphatic diamines mention may be made of hexamethylenediamine, dodecamethylenediamine and trimethylhexamethylenediamine.
• cycloaliphatic diacids mention may be made of 1,4-cyclohexyldicarboxylic acid.
• aliphatic diacids mention may be made of butane-dioic, adipic, azelaic, suberic, sebacic, dodecanedicarboxylic acids, polyoxyalkylenes a,oo-diacids and dimerized fatty acids.
• dimerized fatty acids correspond to the product of the dimerization reaction of fatty acids (generally containing 18 carbon atoms, often a mixture of oleic and/or linoleic acid); they preferably have a dimer content of at least 98%; preferably they are hydrogenated; it is preferably a mixture comprising 0 to 15% by weight of C18 monoacids, 60 to 99% by weight of C36 diacids, and 0.2 to 35% by weight of triacids or polyacids.
• C54 or more these are for example products marketed under the brand "PRIPOL" by the company "CRODA", or under the brand EMPOL by the company BASF, or under the brand Radiacid by the company OLEON.
• terephthalic (T) and isophthalic (I) acids we can cite terephthalic (T) and isophthalic (I) acids.
• cycloaliphatic diamines mention may be made of the isomers of bis-(4-aminocyclohexyl)-methane (BACM), bis-(3-methyl-4-aminocyclohexyl)methane (BMACM) and 2-2-bis- (3-methyl-4-aminocyclohexyl)-propane (BMACP), and para-amino-di-cyclohexyl-methane (PACM).
• BMACM bis-(4-aminocyclohexyl)-methane
• BMACM bis-(3-methyl-4-aminocyclohexyl)methane
• BMACP 2-2-bis- (3-methyl-4-aminocyclohexyl)-propane
• PAM para-amino-di
• polyamide blocks of the third type As examples of polyamide blocks of the third type, the following can be cited:
• PA X/Y, PA X/Y/Z, etc. relate to copolyamides in which X, Y, Z, etc. represent homopolyamide units as described above.
• the polyamide blocks of the copolymer used in the invention comprise (or consist of) blocks of polyamide PA 6, PA 10, PA 11, PA 12, PA 5.4, PA 5.9, PA 5.10, PA 5.12, PA 5.13, PA 5.14, PA 5.16, PA 5.18, PA 5.36, PA 6.4, PA 6.6, PA 6.9, PA 6.10, PA 6.12, PA 6.13, PA 6.14, PA 6.16, PA 6.18, PA 6.36, PA 10.4, PA 10.9, PA 10.10, PA 10.12, PA 10.13, PA 10.14, PA 10.16, PA 10.18, PA 10.36, PA 10.T, PA 12.4, PA 12.9, PA 12.10, PA 12.12, PA 12.13, PA 12.14, PA 12.16, PA 12.18, PA 12.36, PA 12.T, or mixtures or copolymers thereof; and preferably comprise, or consist of, blocks of polyamide PA 6, PA 10, PA 11, PA 12, PA 6.10, PA 6.12, PA 6.13, PA 10.9, PA 10.10, PA 10.12, PA 12.9, or mixtures or copolymers thereof
• Polyether blocks are made up of alkylene oxide units.
• the polyether blocks may in particular be PEG (polyethylene glycol) blocks, i.e. made up of ethylene oxide units, and/or PPG (propylene glycol) blocks, i.e. made up of propylene oxide units, and/or or PO3G (polytrimethylene glycol) blocks, that is to say made up of polytrimethylene glycol ether units, and/or PTMG blocks, that is to say made up of tetramethylene glycol units also called polytetrahydrofuran.
• the polyether blocks of PEBA are blocks of polyethylene glycol and/or polypropylene glycol and/or polytetrahydrofuran.
• PEBA copolymers can include several types of polyethers in their chain, the copolyethers being able to be block or random.
• the polyether blocks can also be made up of ethoxylated primary amines.
• ethoxylated primary amines we can cite the products of formula:
• m and n are integers between 1 and 20 and x an integer between 8 and 18.
• These products are for example commercially available under the brand NORAMOX® from the company CECA and under the brand GENAMIN® from the company CLARIANT.
• the flexible polyether blocks of PEBA include polyoxyalkylene blocks with NH2 chain ends, such blocks being obtainable by cyanoacetylation of aliphatic polyoxyalkylene a,oo-dihydroxylated blocks called polyetherdiols. More particularly, commercial products Jeffamine or Elastamine can be used (for example Jeffamine® D400, D2000, ED 2003,
• the polyetherdiol blocks are thus aminated to be transformed into polyether diamines and condensed with polyamide blocks with carboxylic ends.
• the general method for preparing PEBA copolymers having amide bonds between the PA blocks and the PE blocks is known and described, for example in document EP 1482011.
• the polyether blocks can also be mixed with polyamide precursors and a chain limiter. diacid to prepare polymers with polyamide blocks and polyether blocks having statistically distributed units (one-step process).
• Polyetherdiols with OH chain ends can be present with the aminated polyetherdiols during their condensation with the polyamide blocks.
• These polyetherdiols with OH chain ends can be condensed with polyamide blocks with carboxylic ends, forming ester bonds between the PA blocks and the PE blocks (the products obtained being polyetheresteramides).
• polyetherdiol blocks are copolycondensed with polyamide blocks with carboxylic ends.
• the general method for the two-step preparation of PEBA copolymers having ester bonds between the PA blocks and the PE blocks is known and is described, for example, in document FR 2846332.
• the general method for preparing PEBA copolymers having amide bonds between PA blocks and PE blocks is known and described, for example in document EP 1482011.
• the polyether blocks can also be mixed with polyamide precursors and a diacid chain limiter to prepare polymers with polyamide blocks and polyether blocks having statistically distributed patterns (one-step process).
• PEBA in the present description of the invention relates both to PEBAX® marketed by Arkema, to Vestamid® marketed by Evonik®, to Grilamid® marketed by EMS, and to Pelestat® type PEBA marketed by Sanyo or to any other PEBA from other suppliers.
• the PEBAs which can be used in the invention include copolymers comprising a single polyamide block and a single polyether block, but also copolymers comprising three, four (or even more) different blocks chosen from those described in the present description, since these blocks comprise at least one polyamide block and one polyether block.
• PEBAs which can be used in include copolymers comprising, in addition to polyamide and polyether blocks, one or more blocks of another nature, in particular chosen from the group consisting of polyester blocks, polysiloxane blocks, such as polydimethylsiloxane blocks ( or PDMS), polyolefin blocks, polycarbonate blocks, and mixtures thereof, preferably chosen from the group consisting of polyester blocks, polysiloxane blocks, and mixtures thereof.
• the copolymer may be a segmented block copolymer comprising three different types of blocks (or “triblock”), which results from the condensation of several of the blocks described above.
• Said triblock can for example be a copolymer comprising a polyamide block, a polyester block and a polyether block or a copolymer comprising a polyamide block and two different polyether blocks, for example a PEG block and a PTMG block.
• PEBA copolymers in the context of the invention are copolymers comprising blocks: PA 10 and PEG; PA 10 and PTMG; PA 11 and PEG; PA 11 and PTMG; PA 12 and PEG; PA 12 and PTMG; PA 6.10 and PEG; PA 6.10 and PTMG; PA 6 and PEG; PA 6 and PTMG; PA 6.12 and PEG; PA 6.12 and PTMG.
• the number-average molar mass of the polyamide blocks in the PEBA copolymer is preferably 400 to 20,000 g/mol, more preferably 500 to 10,000 g/mol.
• the number average molar mass of the polyamide blocks in the PEBA copolymer is from 400 to 500 g/mol, or 500 to 600 g/mol, or from 600 to 1000 g/mol, or from 1000 to 1500 g/mol, or from 1500 to 2000 g/mol, or from 2000 to 2500 g/mol, or from 2500 to 3000 g/mol, or from 3000 to 3500 g/mol, or from 3500 to 4000 g/mol, or from 4000 to 5000 g/mol, or from 5000 to 6000 g/mol, or from 6000 to 7000 g/mol, or from 7000 to 8000 g/mol, or from 8000 to 9000 g/mol, or from 9000 to 10000 g /mol, or from 10000 to 11000 g/mol, or from 11000 to 12
• the number average molar mass of the polyether blocks is preferably 100 to 6000 g/mol, more preferably 200 to 3000 g/mol. In embodiments, the number average molar mass of the polyether blocks is from 100 to 200 g/mol, or from 200 to 500 g/mol, or from 500 to 800 g/mol, or from 800 to 1000 g/mol , or from 1000 to 1500 g/mol, or from 1500 to 2000 g/mol, or from 2000 to 2500 g/mol, or from 2500 to 3000 g/mol, or from 3000 to 3500 g/mol, or from 3500 to 4000 g/mol, or from 4000 to 4500 g/mol, or from 4500 to 5000 g/mol, or from 5000 to 5500 g/mol, or from 5500 to 6000 g/mol.
• the number average molar mass is fixed by the chain limiter content. It can be calculated according to the relationship:
• Mn Hmonomer X MWrepeat pattern / H chain limiter + MWchain limiter
• nmonomer represents the number of moles of monomer
• nchain limiter represents the number of moles of diacid limiter in excess
• MW repeat unit represents the molar mass of the repeat unit
• MW chain limiter represents the molar mass of the diacid in excess.
• the number average molar mass of the polyamide blocks and polyether blocks can be measured before copolymerization of the blocks by gel permeation chromatography (GPC).
• the quantity of polyamide blocks in the PEBA is at least 10% by weight and preferably at least 20% by weight (relative to the total weight of the PEBA). Even more advantageously, the quantity of polyamide blocks in the PEBA is at least 30% by weight, more preferably at least 40% by weight, even more preferably at least 50% by weight.
• the quantity of polyamide blocks in the PEBA can be from 10 to 95% by weight (the quantity of polyether blocks preferably being from 5 to 90% by weight), preferably from 30 to 90 by weight (the quantity of polyether blocks being worth preferably 10 to 70% by weight), more preferably 40 to 85% by weight (the quantity of polyether blocks preferably being 15 to 60% by weight).
• the quantity of polyamide blocks in the PEBA can be from 10 to 30% by weight (the quantity of polyether blocks preferably being from 70 to 90% by weight), or from 30 to 40% by weight (the quantity of polyether blocks preferably worth 60 to 70% by weight), or 40 to 50% by weight (the quantity of polyether blocks preferably worth 50 to 60% by weight), or 50 to 60% by weight (the quantity of polyether blocks preferably worth 40 to 50% by weight), or from 60 to 70% by weight (the quantity of polyether blocks preferably worth 30 to 40% by weight), or from 70 to 80% by weight (the quantity of polyether blocks preferably worth from 20 to 30% by weight), or 80 to 95% by weight (the quantity of polyether blocks preferably being 5 to 20% by weight).
• the quantity of polyamide blocks in PEBA can be determined by proton NMR (1 H) in a TFA/CDCIs mixture (1/4 v/v), preferably using a Brucker AM 500 spectrometer, according to the protocol described in the article “Synthesis and characterization of poly(copolyethers-block-polyamides) - II. Characterization and properties of the multiblock copolymers”, Maréchal et al., Polymer, Volume 41, 2000, 3561-3580 (the attribution of the signals being carried out using Figure 5 of said article). These quantities make it possible to obtain a foam having a lower density, greater flexibility and better rebound resilience.
• the PEBA has an NH2 function concentration of 0.01 meq/g to 1 meq/g, preferably of 0.02 meq/g to 0.4 meq/g.
• PEBA can have an NH2 concentration of 0.01 to 0.015 meq/g, or 0.015 to 0.02 meq/g, or 0.02 to 0.025 meq/g, or 0.025 to 0.03 meq/g.
• g or from 0.03 to 0.035 meq/g, or from 0.035 to 0.04 meq/g, or from 0.04 to 0.045 meq/g, or from 0.045 to 0.05 meq/g, or from 0, 05 to 0.06 meq/g, or 0.06 to 0.07 meq/g, or 0.07 to 0.08 meq/g, or 0.08 to 0.09 meq/g, or 0.09 to 0.1 meq/g, or 0.1 to 0.2 meq/g, or 0.2 to 0.3 meq/g, or 0.3 to 0.4 meq/g, or from 0.4 to 0.5 meq/g, or from 0.5 to 0.6 meq/g, or from 0.6 to 0.7 meq/g, or from 0.7 to 0.8 meq/ g, or from 0.8 to 0.9 meq/g, or from 0.9 to 1 meq/g.
• the NH2 function concentration can be measured using a potentiometric dosage according to the following method: a sample of moss is dissolved in metacresol at 80°C, then the NH2 functions of this sample are measured potentiometrically using a solution. of perchloric acid at 0.02N.
• the PEBA can have a COOH function concentration of 0.002 meq/g to 0.2 meq/g, preferably 0.005 meq/g to 0.1 meq/g, more preferably 0.01 meq/g to 0.01 meq/g. 08 meq/g.
• PEBA may have a COOH function concentration of 0.002 to 0.005 meq/g, or of 0.005 to 0.01 meq/g, or of 0.01 to 0.02 meq/g, or of 0.02 to 0.02 meq/g. 0.03 meq/g, or 0.03 to 0.04 meq/g, or 0.04 to 0.05 meq/g, or 0.05 to 0.06 meq/g, or 0.
• the concentration in COOH function can be determined by potentiometric analysis according to the following method: a sample of material is dissolved in alcohol benzylic, then the COOH functions of this sample are measured potentiometrically using a 0.02N tetrabutylammonium hydroxide solution.
• PEBA can also comprise hydroxyl (OH) chain ends (for example coming from the condensation of polyetherdiols with OH chain ends with polyamide blocks with carboxylic ends).
• PEBA can have a concentration of OH function (that is to say hydroxyl chain ends) of 0.002 to 0.2 meq/g, preferably of 0.005 to 0.05 meq/g.
• the concentration of OH function can be determined by proton NMR (1 H) in a TFA/CDCIs mixture (1/4 v/v), preferably using a Brucker AM 500 spectrometer, according to the protocol described in the article “Synthesis and characterization of poly(copolyethers-block-polyamides) - IL Characterization and properties of the multiblock copolymers”, Maréchal et al., Polymer, Volume 41, 2000, 3561-3580 (the attribution of the signals being carried out using Figure 5 of said article).
• the copolymer with polyamide blocks and polyether blocks has a Shore D hardness greater than or equal to 30.
• the copolymer used in the invention has an instantaneous hardness of 65 Shore A to 80 Shore D, more preferably from 75 Shore A to 65 Shore D, more preferably from 80 Shore A to 55 Shore D. Hardness measurements can be carried out according to the ISO 7619-1 standard.
• Thermoplastic polyurethane is a hard-block and soft-block copolymer.
• the term “rigid block” means a block which has a melting point greater than 50°C.
• the presence of a melting point can be determined by differential scanning calorimetry, according to standard ISO 11357-3 Plastics - Differential scanning calorimetry (DSC) Part 3.
• soft block we mean a block having a transition temperature vitreous (Tg) less than or equal to 0°C.
• Tg transition temperature vitreous
• the glass transition temperature can be determined by differential scanning calorimetry, according to standard ISO 11357-2 Plastics - Differential scanning calorimetry (DSC) Part 2.
• Thermoplastic polyurethanes result from the reaction of at least one polyisocyanate with at least one compound reactive with the isocyanate, preferably having two functional groups reactive with the isocyanate, more preferably a polyol, and with a chain extender, optionally in presence of a catalyst.
• the rigid blocks of TPU are blocks made up of units derived from polyisocyanates and chain extenders while the flexible blocks mainly comprise units derived from compounds reactive with isocyanate having a molar mass of between 0.5 and 100 kg/mol, preferably polyols.
• the polyisocyanate may be aliphatic, cycloaliphatic, araliphatic and/or aromatic.
• the polyisocyanate is aliphatic, or aromatic. More advantageously, the polyisocyanate is aliphatic.
• the polyisocyanate is a diisocyanate.
• the polyisocyanate is chosen from the group consisting of tri-, tetra-, penta-, hexa-, hepta- and/or octamethylene diisocyanate, 2-methyl-pentamethylene 1,5-diisocyanate, 2-ethyl- butylene-1,4-diisocyanate, 1,5-pentamethylene diisocyanate, 1,4-butylene-diisocyanate, 1-isocyanato-3,3,5-trimethyl-5-isocyanatomethyl-cyclohexane (isophorone diisocyanate, IPDI), 1,4-bis(isocyanatomethyl)cyclohexane, 1,3-bis(isocyanatomethyl)cyclohexane (HXDI), 2,4-paraphenylene diisocyanate (PPDI), 2,4-tetramethylene xylene diisocyanate (TMXDI), 4 ,4'-, 2,4'-,
• the polyisocyanate is chosen from the group consisting of diphenylmethane diisocyanates (MDI), toluene diisocyanates (TDI), pentamethylene diisocyanate (PDI), hexamethylene diisocyanate (HDI), methylene bis (4-cyclohexyl isocyanate) (HMDI) and mixtures thereof.
• MDI diphenylmethane diisocyanates
• TDI toluene diisocyanates
• PDI pentamethylene diisocyanate
• HDI hexamethylene diisocyanate
• HMDI methylene bis (4-cyclohexyl isocyanate
• the polyisocyanate is 4,4'-MDI (4,4'-diphenylmethane diisocyanate), 1,6-HDI (1,6-hexamethylene diisocyanate) or a mixture thereof. Even more advantageously, the polyisocyanate is 1,6-HDI.
• the compound(s) reactive with isocyanate preferably have an average functionality between 1.8 and 3, more preferably between 1.8 and 2.6, more preferably between 1.8 and 2.2.
• the average functionality of the compound(s) reactive with isocyanate corresponds to the number of functions reactive with isocyanate of the molecules, calculated theoretically for a molecule from a quantity of compounds.
• the isocyanate-reactive compound has, on a statistical average, a Zerewitinoff active hydrogen number in the above ranges.
• the compound reactive with the isocyanate (preferably a polyol) has a number average molar mass of 500 to 100,000 g/mol.
• the compound reactive with the isocyanate may have a number average molar mass of 500 to 8000 g/mol, more preferably of 700 to 6000 g/mol, more particularly of 800 to 4000 g/mol.
• the isocyanate-reactive compound has a number average molar mass of 500 to 600 g/mol, or 600 to 700 g/mol, or 700 to 800 g/mol, or 800 to 800 g/mol.
• the number average molar mass can be determined by GPC, preferably according to ISO 16014-1:2012.
• the compound reactive with the isocyanate has at least one reactive group chosen from the hydroxyl group, the amine group, the thiol group and the carboxylic acid group.
• the compound reactive with the isocyanate has at least one reactive hydroxyl group, more preferably several hydroxyl groups.
• the compound reactive with the isocyanate comprises or consists of a polyol.
• the polyol is chosen from the group consisting of polyester polyols, polyether polyols, polycarbonate diols, polysiloxane diols, polyalkylene diols and mixtures thereof. More preferably, the polyol is a polyether polyol, a polyester polyol and/or a polycarbonate diol, so that the flexible blocks of the thermoplastic polyurethane are polyether blocks, polyester blocks and/or polycarbonate blocks, respectively. More preferably, the flexible blocks of the thermoplastic polyurethane are polyether blocks and/or polyester blocks (the polyol being a polyether polyol and/or a polyester polyol).
• polyester polyol mention may be made of polycaprolactone polyols and/or copolyesters based on one or more carboxylic acids chosen from adipic acid, succinic acid, pentanedioic acid and/or acid sebacic and one or more alcohols chosen from 1,2-ethanediol, 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 3-methyl-1,5-pentanediol, 1,6-hexanediol and/or polytetrahydrofuran.
• carboxylic acids chosen from adipic acid, succinic acid, pentanedioic acid and/or acid sebacic
• alcohols chosen from 1,2-ethanediol, 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 3-methyl-1,5-pentanediol, 1,
• the copolyester may be based on adipic acid and a mixture of 1,2-ethanediol and 1,4-butanediol, or the copolyester may be based on adipic acid, succinic acid, pentanedioic acid, sebacic acid or mixtures thereof, and polytetrahydrofuran (tetramethylene glycol), or the copolyester may be a mixture of these copolyesters.
• polyetherdiols i.e. aliphatic polyoxyalkylene a,oo-dihydroxylated blocks
• the polyether polyol is a polyetherdiol based on ethylene oxide, propylene oxide, and/or butylene oxide, a block copolymer based on ethylene oxide and oxide.
• the polyether polyol is preferably a polytetrahydrofuran (flexible blocks of thermoplastic polyurethane therefore being blocks of polytetrahydrofuran) and/or a polypropylene glycol (flexible blocks of thermoplastic polyurethane therefore being blocks of polypropylene glycol) and/or a polyethylene glycol ( flexible blocks of thermoplastic polyurethane therefore being blocks of polyethylene glycol), preferably a polytetrahydrofuran having a number average molar mass of 500 to 15,000 g/mol, preferably of 1000 to 3000 g/mol.
• the polyether polyol may be a polyetherdiol which is the reaction product of ethylene oxide and propylene oxide; the molar ratio of ethylene oxide relative to propylene oxide is preferably 0.01 to 100, more preferably 0.1 to 9, more preferably 0.25 to 4, more preferably 0 .4 to 2.5, more preferably 0.6 to 1.5 and it is more preferably 1.
• the polysiloxane diols which can be used in the invention preferably have a number average molar mass of 500 to 15,000 g/mol, preferably of 1000 to 3,000 g/mol.
• the number average molar mass can be determined by GPC, preferably according to ISO 16014-1:2012.
• the polysiloxane diol is a polysiloxane of formula (I):
• R is preferably a C2-C4 alkylene
• R' is preferably a C1-C4 alkyl
• each of n, m and p represents independently an integer preferably between 0 and 50, m being more preferably from 1 to 50, even more preferably from 2 to 50.
• the polysiloxane has the following formula (II):
• the polyalkylene diols which can be used in the invention are preferably based on butadiene.
• the polycarbonate diols which can be used in the invention are preferably aliphatic polycarbonate diols.
• the polycarbonate diol is preferably based on alkanediol. Preferably, it is strictly bifunctional.
• the preferred polycarbonate diols are those based on butanediol, pentanediol and/or hexanediol, in particular 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 3-methylpentane-(1, 5)-diol, or mixtures thereof, more preferably based on 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, or mixtures thereof.
• the polycarbonate diol may be a polycarbonate diol based on butanediol and hexanediol, or based on pentanediol and hexanediol, or based on hexanediol, or may be a mixture of two or more of these polycarbonate diols.
• the polycarbonate diol advantageously has a number average molar mass of 500 to 4000 g/mol, preferably of 650 to 3500 g/mol, more preferably of 800 to 3000 g/mol.
• the number average molar mass can be determined by GPC, preferably according to ISO 16014-1:2012.
• One or more polyols may be used as the isocyanate-reactive compound.
• the flexible blocks of the TPU are blocks of polytetrahydrofuran, polypropylene glycol and/or polyethylene glycol.
• a chain extender is used for the preparation of thermoplastic polyurethane, in addition to the isocyanate and the compound reactive with the isocyanate.
• the chain extender may be aliphatic, araliphatic, aromatic and/or cycloaliphatic. It advantageously has a number average molar mass of 50 to 499 g/mol. The number average molar mass can be determined by GPC, preferably according to ISO 16014-1:2012.
• the chain extender preferably has two isocyanate-reactive groups (also called "functional groups"). A single chain extender or a mixture of two or more chain extenders can be used.
• the chain extender is preferably bifunctional.
• chain extenders are diamines and alkanediols having 2 to 10 carbon atoms.
• the chain extender can be chosen from the group consisting of 1,2-ethylene glycol, 1,2-propanediol, 1,3-propanediol, 1,4-butanediol, 2,3-butanediol , 1,5-pentanediol, 1,6-hexanediol, diethylene glycol, dipropylene glycol, 1,4-cyclohexanediol, 1,4-dimethanol cyclohexane, neopentyl glycol, hydroquinone bis (beta-hydroxyethyl ) ether (HQEE), di-, tri-, tetra-, penta-, hexa-, hepta-, octa-, nona- and/or deca-alkylene glycol, their respective oligo
• the chain extender is chosen from the group consisting of 1,2-ethylene glycol, 1,3-propanediol, 1,4-butanediol, 1,5 pentanediol, 1,6-hexanediol, and mixtures thereof, and more preferably it is chosen from 1,3-propanediol, 1,4-butanediol and/or 1,6-hexanediol.
• the chain extender is a mixture of 1,4-butanediol and 1,6-hexanediol, more preferably in a molar ratio of 6:1 to 10:1.
• a catalyst is used to synthesize the thermoplastic polyurethane.
• the catalyst accelerates the reaction between the NCO groups of the polyisocyanate and the isocyanate-reactive compound (preferably with the hydroxyl groups of the isocyanate-reactive compound) and with the chain extender.
• the catalyst is preferably a tertiary amine, more preferably chosen from triethylamine, dimethylcyclohexylamine, N-methylmorpholine, N,N'-dimethylpiperazine, 2-(dimethylaminoethoxy)-ethanol and/or diazabicyclo-(2,2 ,2)-octane.
• the catalyst is an organic metal compound such as an acid ester of titanium, an iron compound, preferably ferric acetylacetonate, a tin compound, preferably those of carboxylic acids, more preferably tin diacetate, tin dioctoate, tin dilaurate or dialkyl tin salts, preferably dibutyltin diacetate and/or dibutyltin dilaurate, a carboxylic acid salt of bismuth, preferably bismuth decanoate, or a mixture thereof.
• an organic metal compound such as an acid ester of titanium, an iron compound, preferably ferric acetylacetonate, a tin compound, preferably those of carboxylic acids, more preferably tin diacetate, tin dioctoate, tin dilaurate or dialkyl tin salts, preferably dibutyltin diacetate and/or dibutyltin dilaurate, a carb
• the catalyst is chosen from the group consisting of tin dioctoate, bismuth decanoate, titanium acid esters and mixtures thereof. More preferably, the catalyst is tin dioctoate.
• the molar ratios of the isocyanate-reactive compound and the chain extender can be varied to adjust the hardness and melt flow index of the TPU. Indeed, when the proportion of chain extender increases, the hardness and melt viscosity of the TPU increase while the fluidity index of the TPU decreases.
• the compound reactive with the isocyanate and the chain extender can be used in a molar ratio of 1: 1 to 1:5, preferably 1:1.5 to 1:4.5, preferably so that the mixture of isocyanate-reactive compound and chain extender has an equivalent weight of hydroxyl greater than 200, more particularly 230 to 650, even more preferably 230 to 500.
• the compound reactive with the isocyanate and the chain extender can be used in a molar ratio of 1:5.5 to 1:15, preferably 1:6 to 1:12, preferably so as to that the mixture of compound reactive with isocyanate and chain extender has a hydroxyl equivalent weight of 110 to 200, more preferably of 120 to 180.
• the polyisocyanate, the compound reactive with the isocyanate and the chain extender are reacted, preferably in the presence of a catalyst, in quantities such that the equivalent ratio of the groups NCO of the polyisocyanate relative to the sum of the hydroxyl groups of the compound reactive with the isocyanate and of the chain extender is from 0.95:1 to 1.10:1, preferably from 0.98:1 to 1, 08:1, more preferably from 1:1 to 1.05:1.
• the catalyst is advantageously present in an amount of 0.0001 to 0.1 parts by weight per 100 parts by weight of the TPU synthesis reagents.
• the TPU preferably has a weight average molar mass greater than or equal to 10,000 g/mol, preferably greater than or equal to 40,000 g/mol and more preferably greater than or equal to 60,000 g/mol. Of preferably, the weight average molar mass of the TPU is less than or equal to 80,000 g/mol. In embodiments, the weight average molar mass of the TPU is from 10,000 to 25,000 g/mol, or from 25,000 to 40,000 g/mol, or from 40,000 to 50,000 g/mol, or from 50,000 to 60,000 g/mol, or from 60,000 to 70,000 g/mol, or from 70,000 to 80,000 g/mol. Weight average molar masses can be determined by gel permeation chromatography (GPC).
• the content of rigid blocks in the TPU is preferably less than or equal to 90% by weight and more preferably less than or equal to 80% by weight (relative to the least total of the TPU). More advantageously, the content of rigid blocks in the TPU is 30 to 60% by weight (the quantity of flexible blocks is 40 to 70% by weight).
• the content of rigid blocks in the TPU can be 10 to 20% by weight (the quantity of flexible blocks being 80 to 90% by weight), or 20 to 30% by weight (the quantity of flexible blocks worth 70 to 80% by weight), or 30 to 40% by weight (the quantity of flexible blocks worth 60 to 70% by weight), or 40 to 50% by weight (the quantity of flexible blocks worth 50 to 60% by weight), or 50 to 60% by weight (the quantity of flexible blocks worth 40 to 50% by weight), or 60 to 70% by weight (the quantity of flexible blocks worth 30 to 40% by weight), or 70 to 80% by weight (the quantity of flexible blocks worth 20 to 30% by weight), or 80 to 90% by weight (the quantity of flexible blocks worth 10 to 20% in weight).
• the content of rigid blocks, expressed as a percentage is defined as follows:
• TPU is semi-crystalline. Its melting temperature Tf is preferably between 100°C and 230°C, more preferably between 120°C and 200°C. The melting temperature can be measured according to ISO 11357-3 Plastics - Differential scanning calorimetry (DSC) Part 3.
• the TPU may be a recycled TPU and/or a partially or completely biosourced TPU.
• the TPU has a hot fluidity index (or MFI for “Melt Flow Index”) of 10 to 100 g/10 min, preferably 25 to 80 g/10 min, more preferably 35 to 65 g/ 10 minutes.
• the hot melt index of the TPU can be from 10 to 25 g/10 min, or from 25 to 35 g/10 min, or from 35 to 45 g/10 min, or from 45 to 55 g/10 min, or 55 to 65 g/10 min, or 65 to 80 g/10 min, or 80 to 100 g/10 min.
• the hot fluid index is measured at 200°C under a load of 10 kg, according to the ASTM D1238 standard.
• the TPU has a Shore D hardness less than or equal to 75, more preferably less than or equal to 65.
• the TPU used in the invention can have a hardness of 65 Shore A to 70 Shore D, preferably of 75 Shore A to 60 Shore D. Hardness measurements can be carried out according to ISO 7619-1.
• the TPU has an OH function concentration of 0.002 meq/g to 0.6 meq/g, preferably 0.01 meq/g to 0.4 meq/g, more preferably 0.03 meq/g. g to 0.2 meq/g.
• the TPU has an OH function concentration of 0.002 to 0.005 meq/g, or of 0.005 to 0.01 meq/g, or of 0.01 to 0.02 meq/g, or of 0.
• concentration of OH function can be determined by proton NMR in DMSO D6, according to the protocol described in the article below: “Reactivity of isocyanates with urethanes: Conditions for allophanate formation”, Lapprand et al., Polymer Degradation and Stability, Volume 90, No. 2, 2005, 363-373.
• the TPU is not crosslinked.
• the quantity of polyamide blocks in the foam is at least 15% by weight, preferably at least 20% by weight, more preferably at least 25% by weight, more preferably at least 30% by weight, more preferably at least 35% by weight (relative to the total weight of the foam).
• the quantity of polyamide blocks in the foam can be determined by proton NMR in a TFA/CDCIs mixture (1/4 v/v), preferably using a Brucker AM 500 spectrometer, according to the protocol described in the article “Synthesis and characterization of poly(copolyethers-block-polyamides) - IL Characterization and properties of the multiblock copolymers”, Maréchal et al., Polymer, Volume 41, 2000, 3561-3580 (the attribution of the signals being carried out using Figure 5 of said article).
• the quantity of rigid blocks of thermoplastic polyurethane in the foam is preferably less than or equal to 50% by weight, more preferably less than or equal to 35% by weight, more preferably less than or equal to 25% by weight, more preferably less than or equal to 15% by weight, relative to the total weight of the foam.
• the quantity of rigid blocks of thermoplastic polyurethane in the foam can be measured in proton NMR in DMSO D6, according to the protocol described in the article: “Reactivity of isocyanates with urethanes: Conditions for allophanate formation”, Lapprand et al., Polymer Degradation and Stability, Volume 90, No. 2, 2005, 363-373.
• the foam according to the invention preferably comprises 40 to 95% by weight of PEBA, and 5 to 60% by weight of TPU, more preferably 50 to 90% by weight of PEBA, and 10 to 50% by weight of TPU, compared to the total weight of the foam. More advantageously, the foam according to the invention comprises from 55 to 80% by weight of PEBA, and from 20 to 45% by weight of TPU, more preferably from 60 to 75% by weight of PEBA, and from 25 to 40% by weight of weight of TPU, compared to the total weight of the foam.
• the foam comprises 40 to 45 weight percent PEBA, and 55 to 60 weight percent TPU, or 45 to 50 weight percent PEBA, and 55 to 50 weight percent TPU , or 50 to 55% by weight of PEBA, and 45 to 50% by weight of TPU, or 55 to 60% by weight of PEBA, and 40 to 45% by weight of TPU, or 60 to 65 % by weight of PEBA, and 35 to 40% by weight of TPU, or 65 to 70% by weight of PEBA, and 30 to 35% by weight of TPU, or 70 to 75% by weight of PEBA, and 25 to 30% by weight of TPU, or 75 to 80% by weight of PEBA, and 20 to 25% by weight of TPU, or 80 to 85% by weight of PEBA, and 15 to 20% by weight of TPU, or 85 to 90% by weight of PEBA, and 10 to 15% by weight of TPU, or 90 to 95% by weight of PEBA, and 5 to 10% by weight of TPU, per relative to the total weight of the foam.
• the foam contains a total content of flexible blocks of the PEBA(s) and the TPU(s) of between 30 and 80% by weight, preferably between 40% and 75% by weight, relative to the total weight of the foam.
• the total soft block content can be determined by nuclear magnetic resonance (NMR), as described above.
• these flexible blocks include PEBA polyether blocks and flexible TPU blocks.
• the molar ratio of the urethane functions to the amine functions NH2 of the assembly consisting of at least one copolymer with polyamide blocks and polyether blocks comprising amine chain ends and at least one thermoplastic polyurethane, in the foam according to the invention can be from 15 to 350, preferably from 25 to 250, even more preferably from 40 to 200.
• concentrations of amine function and urethane function can be determined by 13C NMR in DMSO D6 as described in the article below. below: “Reactivity of isocyanates with urethanes: Conditions for allophanate formation”, Lapprand et al., Polymer Degradation and Stability, Volume 90, N°2, 2005, 363-373.
• the TPU and PEBA foam according to the invention comprises at least part of the total copolymer with polyamide blocks and polyether blocks covalently linked to thermoplastic polyurethane by a urea function.
• the foam according to the invention has a concentration of urea function of 0.001 meq/g to 0.1 meq/g, preferably of 0.003 meq/g to 0.08 meq/g, more preferably of 0.005 meq/g g to 0.05 meq/g.
• concentration of urea function in the foam can be from 0.001 to 0.005 meq/g, or from 0.005 to 0.01 meq/g, or from 0.01 to 0.02 meq/g, or from 0.02 to 0. 03 meq/g, or 0.03 to 0.04 meq/g, or 0.04 to 0.05 meq/g, or 0.05 to 0.08 meq/g, or 0.08 to 0.1 meq/g.
• the concentration of urea function can be measured in 13C NMR in DMSO D6, as described in the article “Reactivity of isocyanates with urethanes: Conditions for allophanate formation”, Lapprand et al., Polymer Degradation and Stability, Volume 90, No. 2, 2005, 363-373.
• the signals corresponding to the carbonyl groups of urethane and urea functions are integrated in order to determine a level of urea function, and the attribution of the signals is made using Figure 6 of said article.
• the foam according to the invention has a concentration in Nhh function of 0.01 meq/g to 1 meq/g, preferably of 0.02 meq/g to 0.4 meq/g.
• the foam may have a concentration based on Nhh of 0.01 to 0.015 meq/g, or of 0.015 to 0.02 meq/g, or of 0.02 to 0.025 meq/g, or of 0.025 to 0.03 meq/g.
• g or from 0.03 to 0.035 meq/g, or from 0.035 to 0.04 meq/g, or from 0.04 to 0.045 meq/g, or from 0.045 to 0.05 meq/g, or from 0, 05 to 0.06 meq/g, or from 0.06 to 0.07 meq/g, or from 0.07 to 0.08 meq/g, or from 0.08 to 0.09 meq/g, or from 0.09 to 0.1 meq/ g, or 0.1 to 0.2 meq/g, or 0.2 to 0.3 meq/g, or 0.3 to 0.4 meq/g, or 0.4 to 0.5 meq/g, or 0.5 to 0.6 meq/g, or 0.6 to 0.7 meq/g, or 0.7 to 0.8 meq/g, or 0.8 to 0 .9 meq/g, or 0.9 to 1 meq/g.
• the NH2 function concentration can be measured using a potentiometric assay. This dosage can for example be carried out as follows: the PEBAs are first dissolved in m-cresol at 80°C then the terminal NH2 functions are determined using a perchloric acid solution.
• the foam according to the invention comprises urea and NH2 functions.
• the foam according to the invention comprises more urea functions than NH2.
• the part of the copolymer with polyamide blocks and polyether blocks covalently linked to thermoplastic polyurethane by a urea function represents 10% or less by weight, more preferably 5% or less by weight, more preferably 3% or less by weight, more preferably 2% or less by weight, of the quantity of the copolymer with polyamide blocks and polyether blocks.
• the foam according to the invention may consist essentially of, or consist of, at least one copolymer with polyamide blocks and polyether blocks and at least one thermoplastic polyurethane and optionally an expanding agent, in the matrix of the foam and/or in the pores of the foam, particularly if it is a closed-pore foam.
• the foam matrix may consist essentially of, or consist of, the at least one TPU and the at least one PEBA.
• the foam may also include degradation products of a blowing agent (particularly in its matrix), particularly when a chemical blowing agent was used to form the foam.
• the foam may comprise one or more additives, for example copolymers of ethylene and vinyl acetate or EVA (for example those marketed under the name Evatane® by SK Chemical), or copolymers of ethylene and acrylate, or copolymers of ethylene and alkyl (meth) acrylate, for example those marketed under the name Lotryl® by SK Chemical.
• additives can make it possible to adjust the hardness of the foamed part, its appearance and its comfort.
• Other additives suitable for the invention include pigments (such as TiO2 and other compatible colored pigments), adhesion promoters (to improve the adhesion of the foam to other materials), fillers (e.g.
• additives may be present in a content of 0 to 30% by weight, preferably from 0.1 to 20% by weight, more preferably from 0.2% to 10% by weight, for example relative to the total weight of the foam.
• the foam does not include crosslinkers.
• the foam is advantageously a non-crosslinked foam.
• the foam according to the invention preferably has a density less than or equal to 800 kg/m 3 , more preferably less than or equal to 600 kg/m 3 , more preferably less than or equal to 400 kg/m 3 , even more preferably less or equal to 300 kg/m 3 , and particularly preferably less than or equal to 230 kg/m 3 . It can for example have a density of 25 to 600 kg/m 3 , and more particularly preferably 50 to 300 kg/m 3 .
• the density of the foam can be from 25 to 100 kg/m 3 , or from 100 to 200 kg/m 3 , or from 200 to 250 kg/m 3 , or from 250 to 300 kg/m 3 , or from 300 to 400 kg/m 3 , or 400 to 500 kg/m 3 , or 500 to 600 kg/m 3 , or 600 to 800 kg/m 3 .
• Density control can be achieved by adapting the parameters of the manufacturing process. Density can be measured at 23°C according to ISO 1183-1.
• the foam according to the invention has an Asker C hardness of 20 to 90, preferably 25 to 70.
• the Asker C hardness of the foam can be from 20 to 25, or from 25 to 30, or from 30 to 40, or 40 to 50, or 50 to 60, or 60 to 70, or 70 to 80, or 80 to 90.
• Asker C hardness can be determined at 23°C, after 15 seconds, according to ISO 7619-1.
• the foam has a rebound resilience greater than or equal to 50%, preferably greater than or equal to 55%. Rebound resilience is measured according to ISO 8307:2007 but using an 18.8g ball.
• this foam has a residual deformation in compression according to standard ISO 7214, less than or equal to 65%, preferably less than or equal to 50%, for example less than or equal to 45%, or less than or equal to 40%, or less than or equal to 35%. The residual deformation is measured after a compression of 25% applied for 70 hours at 23°C followed by relaxation for 30 minutes.
• this foam also has excellent fatigue resistance and cushioning properties.
• this foam also has good resistance to tearing and crack propagation.
• the foam according to the invention can be used to manufacture sports equipment, such as soles of sports shoes, ski boots, midsoles, insoles, or even functional components of soles, in the form of inserts in different parts of the sole (heel or arch for example), or even components of shoe uppers in the form of reinforcements or inserts in the structure of the shoe upper, in the form of protections.
• sports equipment such as soles of sports shoes, ski boots, midsoles, insoles, or even functional components of soles, in the form of inserts in different parts of the sole (heel or arch for example), or even components of shoe uppers in the form of reinforcements or inserts in the structure of the shoe upper, in the form of protections.
• the foam according to the invention has interesting anti-shock, anti-vibration and anti-noise properties, combined with haptic properties adapted to capital goods. It can therefore also be used for the manufacture of railway rail bases, or various parts in the automobile industry, in transport, in electrical and electronic equipment, in construction or in the manufacturing industry.
• the foam objects according to the invention can be easily recycled, for example by melting them in an extruder equipped with a degassing outlet (optionally after having cut them into pieces).
• the foam according to the invention can be prepared by mixing a polymer composition comprising at least one TPU and at least one PEBA comprising amine chain ends with an expanding agent (and optionally with one or more additives), then by carrying out a foaming stage.
• the blowing agent may be a chemical or physical agent, or may also consist of any type of hollow object or any type of expandable microsphere.
• it is a physical agent, such as for example dinitrogen or carbon dioxide, or a hydrocarbon, chlorofluorocarbon, hydrochlorocarbon, hydrofluorocarbon or hydrochlorofluorocarbon (saturated or unsaturated) or a mixture of these.
• butane or pentane can be used.
• it can also be a chemical agent such as for example azodicarbonamide or mixtures based on citric acid and sodium hydrogen carbonate (NaHCOs) (such as the product from the Hydrocerol® range of Clariant).
• a physical blowing agent is used and mixed with the molten polymer composition.
• the physical blowing agent can be in liquid or supercritical form and is then converted to the gas phase during the foaming step. Foaming can be caused by a drop in pressure, for example resulting from the output of an extruder.
• the mixture of the polymer composition and the expanding agent is injected into a mold and foaming is carried out in the mold.
• Foaming can be caused by opening the mold, by underdosing, by the application of gas counter-pressure, by a breathing mold or by a mold equipped with a Variotherm® system.
• foaming techniques that can be used include “batch” foaming, extrusion foaming, such as single-screw or twin-screw extrusion foaming, and microwave foaming.
• the polymer composition comprising TPU and PEBA is prepared prior to its mixing with the expanding agent.
• the polymer composition is an alloy of TPU and PEBA.
• alloy we mean a homogeneous mixture (macroscopically, that is to say to the naked eye).
• the polymer composition can be prepared by a process comprising a step of mixing the copolymer with polyamide blocks and polyether blocks comprising amine chain ends and thermoplastic polyurethane in the molten state.
• a preparation process allows, under certain temperature and mixing time conditions, a reaction to take place between the amine functions of a part of the copolymer with polyamide blocks and polyether blocks and the urethane functions of the TPU, which improves compatibility between polyamide block and polyether block copolymer and thermoplastic polyurethane
• TPU and PEBA can take place in any device for mixing, kneading or extruding plastic materials in the molten state known to those skilled in the art, such as an internal mixer, a cylinder mixer, a extruder, such as a single-screw extruder or a contra- or co-rotating twin-screw extruder, a co-kneader, such as a continuous co-kneader, or a stirred reactor.
• the mixing takes place in an extruder or a co-kneader, more preferably in an extruder, even more preferably in a twin-screw extruder.
• the mixing is carried out at a temperature greater than or equal to 160°C, preferably 160 to 300°C, more preferably 180 to 260°C.
• 160°C preferably 160 to 300°C, more preferably 180 to 260°C.
• the mixing is carried out for a period of 30 seconds to 15 minutes, preferably 40 seconds to 10 minutes.
• the mixing is carried out with stirring.
• the step of mixing the TPU with the PEBA may include mixing the copolymer with polyamide blocks and polyether blocks comprising amine chain ends and thermoplastic polyurethane, in the molten state, with additives.
• the polymer composition can be prepared by introducing the copolymer with polyamide blocks and polyether blocks comprising amine chain ends during the synthesis of the thermoplastic polyurethane.
• the copolymer with polyamide blocks and polyether blocks comprising amine chain ends is used as a compound reactive with isocyanate (as described above in the “Thermoplastic polyurethane (TPU)” section. ), optionally in addition to another compound reactive with the isocyanate, preferably a polyol as described above.
• the preparation process can include the steps of:
• thermoplastic polyurethane that is to say at least one polyisocyanate, at least one chain extender, and optionally at least one compound reactive with the isocyanate;
• thermoplastic polyurethane in the reactor in the presence of the copolymer with polyamide blocks and polyether blocks comprising amine chain ends, so as to obtain the polymer composition.
• Such a preparation process allows the reaction of the NH2 amine functions of a part of the copolymer with polyamide blocks and polyether blocks with the isocyanate functions of a part of the polyisocyanate during the synthesis of the thermoplastic polyurethane, leading to the formation of covalent bonds between the polyamide block and polyether block copolymer and the thermoplastic polyurethane, which improves the compatibility between the polyamide block and polyether block copolymer and the thermoplastic polyurethane.
• the steps of introducing the precursors of the thermoplastic polyurethane and of introducing the copolymer with polyamide blocks and polyether blocks comprising amine chain ends can be simultaneous. or performed in any order.
• a catalyst, in particular as described above, can also be introduced into the reactor.
• the reactor may be a batch reactor, a stirred reactor, a static mixer, an internal mixer, a cylinder mixer, an extruder, such as a single-screw extruder or a contra- or co-rotating twin-screw extruder, a continuous co-kneader , or a combination of these.
• the reactor is an extruder, more preferably a twin-screw extruder.
• the step of synthesizing the thermoplastic polyurethane (in the presence of the copolymer with polyamide blocks and polyether blocks comprising amine chain ends) is carried out at a temperature greater than or equal to 160° C., preferably from 160 to 300° C, more preferably from 180 to 270°C.
• 160° C. preferably from 160 to 300° C, more preferably from 180 to 270°C.
• One or more additives may be introduced into the reactor (at any point in the process) and mixed with the thermoplastic polyurethane and the polyamide block and polyether block copolymer in the reactor.
• the preparation process can include a step of shaping the mixture of TPU and PEBA in the form of granules or powder.
• the mixture is put into powder form, it is preferably first put into the form of granules and then the granules are ground into powder.
• Any type of mill can be used, such as a hammer mill, pin mill, attrition disc mill or impact classifier mill.
• PEBA copolymer comprising blocks of PA 11 with a number average molar mass of 1000 g/mol and blocks of PTMG with a number average molar mass of 1000 g/mol, with hardness 40 Shore D.
• the PEBA copolymer does not include of NH2 functions.
• PEBA copolymer comprising blocks of PA 11 with a number average molar mass of 1000 g/mol and blocks of PTMG with a number average molar mass of 1000 g/mol, with hardness 40 Shore D.
• the PEBA copolymer having a concentration depending on NH2 of 0.032 meq/g.
• TPU TPU with rigid blocks based on 4.4’-MDI and 1.4-BDO (1.4-butanediol) and with flexible polyether blocks (PTMG), hardness 85 Shore A.
• a polymer composition 1 was prepared by mixing 65% by weight of PEBA 1 and 35% by weight of TPU using a ZSK 18 mm twin-screw extruder (Coperion). The temperature of the sheaths was set at 210°C and the speed of the screws was 280 rpm with a flow rate of 8 kg/h. The composition was then dried under reduced pressure at 80°C in order to achieve a humidity level of less than 0.04%.
• a polymer composition 2 was prepared by mixing 65% by weight of PEBA 2 and 35% by weight of TPU using a ZSK 18 mm twin-screw extruder (Coperion). The temperature of the sheaths was set at 210°C and the speed of the screws was 280 rpm with a flow rate of 8 kg/h. The composition was then dried under reduced pressure at 80°C in order to achieve a humidity level of less than 0.04%.
• composition 1 made from composition 1 polymer.
• - Foam 2 (according to the invention): made from polymer composition 2.
• the 15 mm thick foams were prepared using an Arburg Allrounder 520A 150T injection press, with a Trexel series IL type physical blowing agent injection system.
• This machine uses the Mucell® technology with partial opening of the mold (core-back process). The operating parameters are as follows:
• Cooling time 240 s
• the expanding agent used is dinitrogen (N2) introduced at 0.7% by weight.
• - Density characterizes the homogeneity of the foam and corresponds to the difference in density of the foamed part between the point closest to the injection point and the point farthest from the injection point; the lower this quantity, the more homogeneous the foam.
• - Compression test according to ISO 3386-1, measured using a ZWICK compression machine.
• the 50 x 50 x 15 mm foam samples are subjected to four compression cycles until a deformation of 70%, with a displacement speed of 100 mm/min at a temperature of 23°C.
• the measurements at the 4th compression cycle are representative of the intrinsic behavior of the foam and the stresses corresponding to 25, 40 and 50% deformation are noted.
• the concentration in NH2 function can be measured using a potentiometric dosage. This dosage is carried out as follows: the PEBAs are first dissolved in m-cresol at 80°C then the terminal NH2 functions are determined using a perchloric acid solution.
• the foam according to the invention has a lower and more homogeneous density than the comparative foam prepared from composition 1 not comprising amine chain ends.
• the foam according to the invention has greater flexibility, illustrated by the Asker C hardness, and lower compressive stresses than those of the comparative foam, all while having similar rebound resilience.

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• Chemical & Material Sciences (AREA)
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• Chemical Kinetics & Catalysis (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• Engineering & Computer Science (AREA)
• Materials Engineering (AREA)
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• Polyurethanes Or Polyureas (AREA)

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• 2022
  • 2022-10-26 FR FR2211173A patent/FR3141465A1/fr active Pending
• 2023
  • 2023-10-26 EP EP23817797.6A patent/EP4608901A1/de active Pending
  • 2023-10-26 WO PCT/FR2023/051681 patent/WO2024089364A1/fr not_active Ceased
  • 2023-10-26 KR KR1020257016533A patent/KR20250116639A/ko active Pending
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