Classifications

• • 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
  • C08L77/02—Polyamides derived from omega-amino carboxylic acids or from lactams thereof
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L51/00—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
  • C08L51/06—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers grafted on to homopolymers or copolymers of aliphatic hydrocarbons containing only one carbon-to-carbon double bond
• • 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
  • C08L77/06—Polyamides derived from polyamines and polycarboxylic acids
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L2205/00—Polymer mixtures characterised by other features
  • C08L2205/02—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L2205/00—Polymer mixtures characterised by other features
  • C08L2205/02—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
  • C08L2205/025—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L2205/00—Polymer mixtures characterised by other features
  • C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L2205/00—Polymer mixtures characterised by other features
  • C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
  • C08L2205/035—Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L2205/00—Polymer mixtures characterised by other features
  • C08L2205/06—Polymer mixtures characterised by other features having improved processability or containing aids for moulding methods

Definitions

• thermoplastic composition with greater melt flowability.
• the present invention relates to shock-modified polyamide thermoplastic compositions comprising at least one prepolymer having a greater melt flowability than a prepolymer-free composition, while maintaining the same modulus and impact properties. It also relates to its use for extrusion, injection, in particular for the manufacture of articles obtained by extrusion, injection, in particular for the manufacture of sports shoes, especially ski or running shoes, or molding by compression.
• the invention also relates to the use of prepolymers with impact modified polyamide thermoplastic dies to increase melt flowability.
• the invention also relates to a method of manufacturing said sports articles and the articles obtained by said method.
• Thermoplastic compositions based on polyamide are raw materials that can be processed by extrusion, molding or injection, in particular by injection molding to manufacture plastic parts. There are several major properties that are desired for these polyamide-based compositions, especially when used in these transformation processes.
• EP 1568487 discloses molded articles comprising:
• a resin member which comprises a resin of the polyamide series which may be a resin composition containing a resin of the polyamide series and a compound having an amino group comprising at least one polyamide oligomer, and
• EP 0272695 discloses compositions comprising a blend of a high molecular weight polyamide with a low molecular weight polyamide in the presence of impact modifiers to obtain an intermediate average molecular weight polyamide by transamidation.
• WO 2006/079890 discloses compositions comprising from 95 to 10 parts by weight of a polyamide having a number average molecular weight greater than 30,000 g / mol and from 5 to 90 parts by weight of a polyamide having an average molecular weight in number from 15,000 to 30,000 g / mol.
• a composition comprising functionalized polyolefins, with or without addition of ungrafted polyolefins, said composition having a high viscosity, makes it possible to improve the fluidity of the latter and thus obtain a fluidity or a rheological behavior compatible with the shaping processes of interest, such as injection molding.
• the present invention relates to a composition comprising:
• composition having a greater melt flowability than the same prepolymer-free composition, the number-average molecular weight of the polyamide of said composition being substantially identical in the presence or absence of said prepolymer.
• substantially identical means that the average molecular weight of said polyamide does not increase by more than 10% in the presence or absence of prepolymer.
• polyamide should be understood in the broad sense of the term and containing amide functions resulting from a polycondensation reaction between the carboxylic acid and amine functions.
• copolymers or copolyamides, based on different amide units, such as for example copolyamide 6/12 with amide units derived from lactam-6 and lactam-12.
• Aliphatic polyamides linear or branched, cycloaliphatic polyamides, semi-aromatic polyamides, aromatic polyamides:
• the polyamides are obtained from an aminocarboxylic acid (also called an amino acid), a lactam or a unit corresponding to the formula XY, X being a diamine in Ca and Y being a diacid in Cb, also called (diamine in Ca). (diacid in Cb), with a representing the number of carbon atoms of the diamine and b representing the number of carbon atoms of the diacid, a and b being each ranging from 4 to 36.
• an aminocarboxylic acid also called an amino acid
• a lactam or a unit corresponding to the formula XY
• X being a diamine in Ca
• Y being a diacid in Cb, also called (diamine in Ca).
• (diacid in Cb) with a representing the number of carbon atoms of the diamine and b representing the number of carbon atoms of the diacid, a and b being each ranging from 4 to 36.
• the polyamide When the polyamide is obtained from a unit derived from an amino acid, it may be chosen from 9-aminononanoic acid, 10-aminodecanoic acid, 10-aminoundecanoic acid and 11-aminoundecanoic acid. and 12-aminododecanoic acid and its derivatives, especially N-heptyl-1-aminoundecanoic acid.
• the polyamide is obtained from a unit derived from a unit having the formula (diamine Ca).
• the unit (diamine Ca) is selected from linear or branched aliphatic diamines, cycloaliphatic diamines and alkylaromatic diamines.
• the diamine When the diamine is aliphatic and branched, it may have one or more methyl or ethyl substituents on the main chain.
• the monomer (diamine in Ca) may advantageously be chosen from 2,2,4-trimethyl-1,6-hexanediamine, 2,4,4-trimethyl-1,6-hexanediamine, 1,3 diaminopentane, 2-methyl-1,5-pentanediamine, 2-methyl-1,8-octanediamine.
• the monomer (diamine Ca) is alkylaromatic, it is preferably selected from 1,3-xylylenediamine and 1,4-xylylenediamine.
• the pattern (diacid Cb) is selected from linear or branched aliphatic diacids, cycloaliphatic diacids and aromatic diacids.
• the fatty acid dimers mentioned above are dimerized fatty acids obtained by oligomerization or polymerization of unsaturated monobasic fatty acids with a long hydrocarbon chain (such as linoleic acid and oleic acid), as described in particular in the document EP 0 471 566.
• the diacid when it is cycloaliphatic, it may comprise the following carbon skeletons: norbornyl methane, cyclohexylmethane, dicyclohexylmethane, dicyclohexylpropane, di (methylcyclohexyl), di (methylcyclohexyl) propane.
• the diacid is aromatic, it is preferably selected from terephthalic acid (noted T), isophthalic acid (noted I) and naphthalenic diacids.
• the polyamide is obtained from a single aminocarboxylic acid, a single lactam or a single X.Y.
• this polyamide a mixture of two or more aminocarboxylic acids, a mixture of two or more lactams, but also a mixture of one, of two or more aminocarboxylic acids with one, two or more lactams.
• the second lactam or amino acid represents up to 30% by weight of the sum of the two lactams or amino acid.
• each monomer of the X.Y unit may be substituted by another monomer X 'and / or Y', different from X or Y.
• the second monomer X 'and / or Y' represents up to 30% by weight of the sum X + X 'and / or Y + Y'.
• Peba are copolymers (A) with amide units (Aa1) and polyether units (Aa2) which result from the copolycondensation of sequences polyamides with reactive ends with polyether sequences with reactive ends, such as, inter alia:
• the copolymers of the invention are advantageously of this type.
• the polyamide sequences with dicarboxylic chain ends come for example from the condensation of polyamide precursors in the presence of a dicarboxylic acid chain limiter.
• Polymers with polyamide blocks and polyether blocks may also comprise randomly distributed units. These polymers can be prepared by the simultaneous reaction of the polyether and the precursors of the polyamide blocks.
• polyetherdiol, polyamide precursors and a chain-limiting diacid can be reacted.
• the amide unit (Aa1) corresponds to an aliphatic repeating unit as defined above for the polyamide.
• (Aa1) represents 11-aminoundecanoic acid or undecanolactam.
• the polyether units are especially derived from at least one polyalkylene ether polyol
• the number-average molecular mass of the polyether blocks is advantageously from 200 to 4000 g / mol, preferably from 250 to 2500 g / mol, especially from 300 to 1100 g / mol.
• the copolymer (A) can be prepared by the following process:
• the comonomer or comonomers selected from lactams and alpha-omega aminocarboxylic acids;
• the formation reaction of the block (Aa1) is usually between 180 and 300 ° C, preferably from 200 to 290 ° C, the pressure in the reactor is between 5 and 30 bar, and is maintained about 2 to 3 hours. The pressure is slowly reduced by putting the reactor at atmospheric pressure, then the excess water is distilled for example for one hour or two.
• the carboxylic acid terminated polyamide having been prepared, the polyether and a catalyst are then added.
• the polyether can be added in one or several times, the same for the catalyst.
• the polyether is first added, the reaction of the OH ends of the polyether and the COOH ends of the polyamide begins with the formation of ester bonds and elimination of water. As much water as possible is removed from the reaction medium by distillation, and then the catalyst is introduced to complete the bonding of the polyamide blocks and the polyether blocks.
• This second step is carried out with stirring, preferably under a vacuum of at least 15 mmHg (2000 Pa) at a temperature such that the reagents and copolymers obtained are in the molten state.
• this temperature can be between 100 and 400 ° C and most often 200 and 300 ° C.
• the reaction is monitored by measuring the torque exerted by the molten polymer on the stirrer or by measuring the electrical power consumed by the stirrer. The end of the reaction is determined by the value of the target torque or power.
• antioxidant it may also be added during the synthesis, at the time deemed most appropriate, one or more molecules used as an antioxidant, for example Irganox® 1010 or Irganox® 245.
• said dicarboxylic acid is used as chain limiter, which is introduced in excess relative to the stoichiometry of the diamine or diamines.
• the catalyst used is a derivative of a metal selected from the group consisting of titanium, zirconium and hafnium or a strong acid such as phosphoric acid, hypophosphorous acid or boric acid.
• the polycondensation can be conducted at a temperature of 240 to 280 ° C.
• copolymers with known ether and amide units consist of linear and semi-crystalline aliphatic polyamide sequences (for example "Pebax®” from Arkema).
• prepolymer refers to oligomers of polyamides necessarily of number average molecular weight less than that of the polyamides used in the matrix, in particular said prepolymer with a number average molecular weight of from 1000 to 10000 g / mol.
• the prepolymer may be chosen from oligomers of linear or branched aliphatic polyamides, oligomers of cycloaliphatic polyamides, oligomers of semi-aromatic polyamides, oligomers of aromatic polyamides, linear or branched aliphatic polyamides, cycloaliphatic and semi-aromatic polyamides. aromatics having the same definition as above.
• the prepolymer may also be a copolyamide oligomer or a mixture of oligomers of polyamides and copolyamide.
• the impact modifier is advantageously constituted by a polymer having a flexural modulus of less than 100 MPa measured according to the ISO 178 standard and Tg of less than 0 ° C. (measured according to the standard 1 1357-2 at the point of inflection of the DSC thermogram), in particular a polyolefin, coupled or not with a Peba having a flexural modulus ⁇ 200 MPa.
• the impact modifier polyolefin may be functionalized or non-functionalized or be a mixture of at least one functionalized and / or at least one non-functionalized.
• the polyolefin has been designated by
• a non-functionalized polyolefin (B2) is conventionally a homopolymer or copolymer of alpha olefins or diolefins, such as, for example, ethylene, propylene, butene-1, octene-1, butadiene.
• alpha olefins or diolefins such as, for example, ethylene, propylene, butene-1, octene-1, butadiene.
• LDPE low density polyethylene or linear low density polyethylene
• LLDPE linear low density polyethylene or linear low density polyethylene
• VLDPE very low density polyethylene or very low density polyethylene
• metallocene polyethylene metallocene polyethylene
• ethylene / alpha-olefin copolymers such as ethylene / propylene, EPR (abbreviation of ethylene-propylene-rubber) and ethylene / propylene / diene (EPDM).
• EPR abbreviation of ethylene-propylene-rubber
• EPDM ethylene / propylene / diene
• SEBS Styrene / ethylene-butene / styrene block copolymers
• SBS styrene / butadiene / styrene
• SIS styrene / isoprene / styrene
• SEPS styrene / ethylene-propylene / styrene
• unsaturated carboxylic acid salts or esters such as alkyl (meth) acrylate (for example methyl acrylate), or vinyl esters of carboxylic acids Saturated such as vinyl acetate (EVA), the proportion of comonomer up to 40% by weight.
• the functionalized polyolefin (B1) may be a polymer of alpha olefins having reactive units (functionalities); such reactive units are acid, anhydride or epoxy functions.
• reactive units are acid, anhydride or epoxy functions.
• 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, especially maleic anhydride, according to a degree of grafting, for example from 0.01 to 5% by weight.
• the functionalized polyolefin (B1) may be chosen from the following (co) polymers, grafted with maleic anhydride or glycidyl methacrylate, in which the degree of grafting is, for example, from 0.01 to 5% by weight:
• PE polystyrene
• PP polystyrene
• ethylene / alpha-olefin copolymers such as ethylene / propylene, EPR (abbreviation of ethylene-propylene-rubber) and ethylene / propylene / diene
• EVA ethylene-vinyl acetate copolymers
• the functionalized polyolefin (B1) may also be chosen from ethylene / propylene predominantly propylene copolymers grafted with maleic anhydride and then condensed with monoamino polyamide (or a polyamide oligomer) (products described in EP-A-0342066). .
• the functionalized polyolefin (B1) may also be a copolymer or copolymer of at least the following units: (1) ethylene, (2) alkyl (meth) acrylate or saturated carboxylic acid vinyl ester and (3) anhydride such as maleic anhydride or (meth) acrylic acid or epoxy such as glycidyl (meth) acrylate.
• ethylene is preferably at least 60% by weight and in which the monomer ter (the function) represents, for example, from 0.1 to 10% by weight of the copolymer: ethylene / alkyl (meth) acrylate / (meth) acrylic acid or maleic anhydride or glycidyl methacrylate copolymers;
• the (meth) acrylic acid may be salified with Zn or Li.
• alkyl (meth) acrylate in (B1) or (B2) refers to C1-C8 alkyl methacrylates and acrylates, and may be selected from methyl acrylate, ethyl acrylate, and the like. , n-butyl acrylate, iso-butyl acrylate, 2-ethylhexyl acrylate, cyclohexyl acrylate, methyl methacrylate and ethyl methacrylate.
• polyolefins (B1) can also be crosslinked by any suitable method 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 that can react with one another.
• a difunctional reagent such as diacid, dianhydride, diepoxy, etc. capable of reacting with them or mixtures of at least two functionalized polyolefins that can react with one another.
• copolymers mentioned above, (B1) and (B2) can be copolymerized randomly or sequentially and have a linear or branched structure.
• MFI molecular weight
• density of these polyolefins can also vary to a large extent, which the skilled person will appreciate.
• MFI abbreviation of Melt Flow Index, is the melt flow index. It is measured according to ASTM 1238.
• the non-functionalized polyolefins (B2) are chosen from homopolymers or copolymers of polypropylene and any homopolymer of ethylene or copolymer of ethylene and a comonomer of higher alpha olefinic type such as butene or hexene. octene or 4-methyl-1-pentene.
• PP high density PE
• medium density PE linear low density PE
• low density PE PE very low density.
• These polyethylenes are known to those skilled in the art as being produced according to a "radical” process, according to a "Ziegler” type of catalysis or, more recently, according to a "metallocene” catalysis.
• the functionalized polyolefins (B1) are chosen from any polymer comprising alpha olefinic units and units carrying polar reactive functional groups such as the epoxy, carboxylic acid or carboxylic acid anhydride functions.
• examples of such polymers include the ter polymers of ethylene, alkyl acrylate and maleic anhydride or glycidyl methacrylate such as Lotader ® of the Applicant or polyolefins grafted with maleic anhydride as Orevac ® of the Applicant as well as ter polymers of ethylene, of alkyl acrylate and of (meth) acrylic acid. Mention may also be made of homopolymers or copolymers of polypropylene grafted with a carboxylic acid anhydride and then condensed with polyamides or monoamino oligomers of polyamide.
• the MFI of the polyamide, the MFI of (B1) and (B2) can be chosen from a wide range; however, it is recommended to facilitate the dispersion of (B) that the MFI of the polyamide is greater than that of (B).
• the composition may also comprise up to 20% by weight, relative to the total weight of the composition, of an additive chosen from antistatic fillers, nucleants, lubricants, dyes, pigments, brighteners, oxidizing agents, fibers, in particular aramid fibers, glass fibers, carbon fibers, advantageously glass fibers, fillers, in particular silica, graphite, expanded graphite, carbon black, balls glass, kaolin, magnesia, slag, talc, wollastonite, nanofillers (carbon nanotubes) and stabilizers.
• an additive chosen from antistatic fillers, nucleants, lubricants, dyes, pigments, brighteners, oxidizing agents, fibers, in particular aramid fibers, glass fibers, carbon fibers, advantageously glass fibers, fillers, in particular silica, graphite, expanded graphite, carbon black, balls glass, kaolin, magnesia, slag, talc, wollastonite, nanofillers (carbon nanotube
• the usual stabilizers used with polymers are phenols, phosphites, UV absorbers, stabilizers of HALS (Hindered Amine Light Stabilizer) type, metal iodides, etc. Examples include Irganox 1010, 245, 1098, Irgafos 168, Tinuvin 312, Iodide P201 from Ciba.
• HALS Hindered Amine Light Stabilizer
• Irganox 1010, 245, 1098, Irgafos 168, Tinuvin 312, Iodide P201 from Ciba The Applicant has therefore surprisingly found that the introduction of a prepolymer into a PA / impact modifier composition thus leads to a more fluid melt composition than the same composition without prepolymers, the number-average molecular weight of the polyamide said composition being substantially identical in the presence or absence of said prepolymer.
• Another advantage of the invention besides the greater fluidity of the compositions, is that the impact properties and flexural rigidity are not impaired in comparison with the properties of the same compositions without prepolymer.
• composition of the invention is devoid of thermoplastic polyurethanes.
• the polyamide of the matrix is predominant with respect to the total of the polyamides present in the composition.
• the polyamide of the matrix present in the composition is an aliphatic polyamide, in particular a long-chain polyamide, such as
• PA1 1 PA12, or an XY polyamide, in particular PA10.10, PA10.12 or PA12.12, or a short-chain polyamide such as PA6, 6.6 or 6.10, in particular the polyamide, is chosen from PA6 and PA1 1.
• Homopolyamides and copolyamides are distinguished by their number of carbon atoms per nitrogen atom, knowing that there are as many nitrogen atoms as amide groups (-CO-NH-).
• the number of carbon atoms per nitrogen atom is the average of the X unit and the Y unit.
• said prepolymer corresponds to a polyamide, in particular an aliphatic one, in particular chosen from PA6, PA1 1, PA12 and PA6 / 12 or a mixture of these.
• a single prepolymer is used in the composition.
• Said prepolymer may have a number-average molecular weight of from 1000 to 10000 g / mol, especially from 1000 to 9000 g / mol, especially from 1000 to 8000 g / mol, in particular from 1000 to 7000 g / mol, especially from 1000 to 1000 g / mol. 6000 g / mole, in particular from 1000 to 5000 g / mole, in particular from 2000 to 5000 g / mole, in particular from 2000 to 4000 g / mole, in particular from 2000 to 3000 g / mole, preferably 2500 g / mole.
• the proportion by weight of prepolymer is from 0.1 to 20%, especially from 1 to 20%, especially from 3 to 20%, especially from 3 to 15%, relative to the total of the composition.
• the proportion by weight of prepolymer is from 1 to 30%, especially from 3 to 25% relative to the weight of prepolymer-polyamide.
• the proportion by weight of prepolymer is from 0.1% to 6% by weight relative to the weight of prepolymer-polyamide.
• the ratio: viscosity at a shear rate of 100 sec -1 of a composition without prepolymer / viscosity of a composition with prepolymer is at least 1, 6, in particular at least 1, 6 to approximately 5, as determined by capillary rheometry on Rheo_tester 2000 Gottfert at 260 ° C).
• the compositions of the invention have a fluidity dependent on the prepolymer concentration introduced and greater than that of a prepolymer-free composition.
• the ratio: flexural modulus at 23 ° C. of a composition without prepolymer / flexural modulus at 23 ° C. of a composition with a prepolymer is about 1, as determined according to ISO 178: 2010.
• the ratio: impact notched at -30 ° C of a composition without prepolymer / impact notched at -30 ° C of a composition with prepolymer is about 1, as determined according to ISO 179-1: 2010 eA.
• compositions of the invention have a viscosity ratio of at least 1.6, in particular from at least 1.6 to about 5, and a flexural modulus ratio of about 1 and a ratio of notched shock of about 1, these three ratios being as defined above.
• the prepolymer present does not affect the properties, especially of modulus and shock, of the polyamide with which it is introduced into the composition.
• the prepolymer may comprise a carbon number per nitrogen atom different from that of the polyamide, or identical to that of the polyamide or close to that of the polyamide.
• the polyamide and the prepolymer can therefore both be long chain or both short chain or the polyamide is long chain and the short chain prepolymer, or the polyamide is short chain and the prepolymer is long chain .
• the prepolymer is chosen from short-chain polyamides and is compatible with the polyamide of the matrix, in particular the polyamide of the matrix is chosen from short-chain polyamides.
• the short-chain prepolymer and the polyamide of the short-chain matrix may be selected from the following: 6, 4.6, 6.6, 6.T, 6.1, 6.10, 6.12, 9.T, 9T, 9 'denoting 2-methyl -1,8-octanediamine, ie the isomer of diamine-9 or 1, 9-nonanediamine, 6 / 6.6, 6.T / 6.6, 6.T / 6.I / 6.6.
• the prepolymer consists of PA6 and the polyamide is a short chain PA, in particular a PA6, PA6.Y, Y representing a C4 to C12 diacid, especially a PA6.10 or PA6.12.
• the prepolymer consists of a PA6 / 12 copolymer and the polyamide is a short chain PA, in particular PA6 or PA6.12. It is obvious that the ratio of monomers in copolyamide PA6 / PA12 can range from 0.1 / 99.9 to 99.9 / 0.1 by weight.
• the prepolymer is chosen from long-chain polyamides and is compatible with the polyamide of the matrix, in particular the polyamide of the matrix is chosen from long-chain polyamides, in particular aliphatic polyamides, semi-aromatic or cycloaliphatic.
• the long-chain prepolymer and the polyamide of the long-chain matrix may be selected from the following: 12, 11, 10.10, 10.12, 6.18, 10.T, 12.T, 12 / 10.T, 12.12, 10.10 / 10.12 and 10.10 / 10.T
• the impact modifier used in the composition is chosen from a polyolefin or a mixture of several polyolefins or a non-reactive Peba.
• some or all of the polyolefins carry a functional group chosen from carboxylic acid, carboxylic anhydride and epoxide functions, and is in particular chosen from an ethylene-propylene copolymer with an elastomeric nature (EPR), an ethylene-propylene copolymer with an elastomeric nature (EPDM) and an ethylene / alkyl (meth) acrylate copolymer, a higher ethylene-alkene copolymer, in particular an ethylene-octene copolymer, an ethylene-alkyl acrylate-maleic anhydride terpolymer.
• EPR ethylene-propylene copolymer with an elastomeric nature
• EPDM ethylene-propylene copolymer with an elastomeric nature
• EPDM ethylene / alkyl (meth) acrylate copolymer
• ethylene / alkyl (meth) acrylate copolymer a higher ethylene-al
• the impact modifier is chosen from F493, a Lotader®, in particular Lotader 5500 or Lotader 7500, VA1803, or a mixture of these, in this case they are in a ratio of 0.1 / 99.9 to 99.9 / 0.1, preferably 1/2 to 2/1 when in a mixture of two.
• the impact modifier is chosen from the following mixtures: F493 / Lotader®, in particular F493 / Lotader® 5500 or F493 / Lotader® 7500.
• the impact modifier in the composition of the invention is present in proportion of 5 to 45% by weight, in particular of 10 to 30% by weight, in particular of 15 to 30% by weight relative to the total weight of the composition.
• the additives of the composition are chosen from stabilizers, dyes, plasticizers, fibers, fillers and impact modifiers other than polyolefins.
• the invention relates to the use of a composition as defined above, for the manufacture of articles obtained by extrusion, injection or molding.
• the articles obtained by extrusion may be tubes or pipes for dispensing fluids, in particular gasoline, compressed air or refrigerant fluids.
• the articles obtained by injection are for example sports articles, especially sports shoes and especially ski boots or running shoes.
• the articles obtained by molding can be tanks, in particular fuel tanks or gas.
• the present invention relates to a process for the preparation of articles as defined above, comprising a step of extruding, injecting or molding the composition defined above.
• the present invention relates to articles as obtained by the method defined above.
• the polyamide composition used in the invention can be prepared by compounding the polyamide of the matrix, the prepolymer and the impact modifier, optionally the mold release agent as well as any other components.
• the composition is usually recovered in the form of pellets or granules.
• the invention relates to the use of a prepolymer with a matrix consisting of at least one polyamide, a shock modifier and optionally an additive, to constitute a composition having a greater fluidity in the molten state than the same composition devoid of prepolymer and whose polyamide has a number-average molecular weight substantially identical in the presence or absence of said prepolymer, said polyamide being present in a proportion of 45 to 94.95% by weight, in particular 55 to 94.95%;
• said prepolymer being present in a proportion of from 0.05% to 20% by weight, the proportion by weight of polyamide matrix and that of prepolymer being respectively from 60 to 99.9% and from 40 to 0.1%, relative to the sum polyamide-prepolymer;
• said impact modifier being present in a proportion of 5 to 45% by weight; and said additive being in proportion by weight of 0 to 20%,
• the sum of the polyamide, the prepolymer of the impact modifier and optionally additives being equal to 100%.
• the polyamide, the prepolymer, the impact modifier and the additive being as defined above.
• the prepolymer reacts preferentially with the impact modifier and not with the polyamide when it is mixed with a shock modifier and a polyamide and therefore there is no transamidation reaction of the prepolymer with the polyamide.
• the number-average molecular weight of the polyamide is therefore substantially identical in the presence or absence of said prepolymer.
• said composition is devoid of resin of the series of polyurethanes.
• the present invention relates to a process for preparing a composition
• a process for preparing a composition comprising contacting a prepolymer with a matrix consisting of at least one polyamide, a shock modifier and optionally an additive,
• said polyamide being present in a proportion of 45 to 94.95% by weight
• said prepolymer being present in a proportion of from 0.05% to 20% by weight, the proportion by weight of polyamide matrix and that of prepolymer being respectively from 60 to 99.9% and from 40 to 0.1%, relative to the sum polyamide-prepolymer;
• said impact modifier being present in a proportion of 5 to 45% by weight; and said additive being in proportion by weight of 0 to 20%, the sum of the polyamide, the prepolymer of the impact modifier and optionally additives being equal to 100%,
• composition having a greater melt flowability than the same prepolymer-free composition and the number-average molecular weight of the polyamide of said composition being substantially identical in the presence or absence of said prepolymer, said process being free of transamidation reaction between said prepolymer and said polyamide.
• prepolymer The contacting of the three constituents: prepolymer, polyamide and impact modifier, is carried out simultaneously, thus allowing the prepolymer to react preferentially with the impact modifier and not to make a transamidation reaction with the polyamide whose number-average molecular mass is therefore substantially identical in the presence or absence of said prepolymer.
• FIG. 1 shows the capillary rheometry on Rhéo_tester 2000 Gottfert at 260 ° C. of compositions of the invention consisting of variable amounts of PA6 (proportions of 60 to 70% by weight) and impact modifier (Lotader 7500: 10% by weight and Fusabond F493: 20% by weight) in the presence of variable amounts of PA6 prepolymer (from 0 to 10% by weight).
• FIG. 2 shows the capillary rheometry on Rhéo_tester 2000 Gottfert at 260 ° C. of compositions of the invention consisting of PA6 (proportions of 55 to 70% by weight) and impact modifier (Lotader 5500: 10% by weight and Fusabond F493 20% by weight) in the presence of variable amounts of PA6 prepolymer.
• PA6 proportions of 55 to 70% by weight
• impact modifier Litader 5500: 10% by weight and Fusabond F493 20% by weight
• Figure 3 shows the capillary rheometry on Rhéo_tester 2000 Gottfert at 260 ° C
• compositions of the invention (PA1 1 and 20% impact modifier: F493 fusabond) in the presence or absence of 3% by weight of PA1 prepolymer 1)
• Figure 4 shows the capillary rheometry on Rhéo_tester 2000 Gottfert at
• compositions of the invention PA1 1 and 15% impact modifier: F493 fusabond in the presence or absence of 3% by weight of PA1 1 prepolymer
• Abscisse Corrected shear gradient Rabinowitsch (s "1 )
• FIG. 5 shows the capillary rheometry on Rhéo_tester 2000 Gottfert at 260 ° C. of compositions of the invention (PA6.10, 30% of impact modifier: Tafmer MH5020 15% and incurs 8200 15%, in the presence or absence of 3% by weight). prepolymer weight PA6)
• FIG. 6 shows the capillary rheometry on Rhéo_tester 2000 Gottfert at 260 ° C. of compositions of the invention (PA6.10, 30% Tafmer MH5020 impact modifier in the presence or absence of 3% by weight of PA6 prepolymer)
• FIG. 7 shows the capillary rheometry on Rhéo_tester 2000 Gottfert at 260 ° C. of compositions of the invention (PA10.10, 30% of impact modifier: Tafmer MH5020 15% and incurs 8200 15%, in the presence or absence of 3% by weight).
• FIG. 8 shows the capillary rheometry on Rhéo_tester 2000 Gottfert at 260 ° C. of compositions of the invention (PA10.10, 30% of Tafmer MH5020 shock modifier in the presence or absence of 3% by weight of PA1 1 prepolymer)
• Lotader 7500 and 5500 ethylene / alkyl acrylate / maleic anhydride terpolymer marketed by the Applicant.
• Exxelor TM VA 1803 copolymer of ethylene and propylene grafted maleic anhydride marketed by Exxon Mobil Chemical.
• Tafmer MH5020 maleic anhydride grafted ethylene-butene copolymer (MAH) marketed by Mitsui Chemicals
• a polyamide 11 (KNO, matrix)
• PA1 1 (KNO) + 20% F493 + 3% prepolymer PA1 1
• PA1 1 (KNO, matrix) + 15% F493 + 3% prepolymer PA1 1
• PA1 1 (KNO, matrix) + 15% VA1803 + 3% prepolymer PA1 1
• PA6 / PA6 prepolymer 85.7 / 14.3
• compositions of the invention based on PA 10.10
• Machine temperature 240 ° C.
• Speed of the screw 300 rpm.
• Bars 80x10x4 mm 3 were made by injection molding. The following process parameters were used:
• This example shows that the average molecular weight of a PA 1 1 brought into contact with a shock modifier or simultaneously with an impact modifier and a prepolymer is substantially identical, regardless of the average molecular weight at the origin of PA 1 1 showing that there is no transamidation reaction between the prepolymer and the polyamide.

Landscapes

• Chemical & Material Sciences (AREA)
• Health & Medical Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• Compositions Of Macromolecular Compounds (AREA)
• Injection Moulding Of Plastics Or The Like (AREA)

Applications Claiming Priority (2)

Publications (1)

Family

ID=51168105

Family Applications (1)

Country Status (7)

Families Citing this family (9)

Citations (1)

Family Cites Families (24)

• 2014
  • 2014-04-02 FR FR1452901A patent/FR3019553B1/fr active Active
• 2015
  • 2015-03-31 JP JP2016559646A patent/JP7084107B2/ja active Active
  • 2015-03-31 KR KR1020167026433A patent/KR102277345B1/ko active IP Right Grant
  • 2015-03-31 WO PCT/FR2015/050825 patent/WO2015150687A1/fr active Application Filing
  • 2015-03-31 EP EP15717047.3A patent/EP3126448A1/de active Pending
  • 2015-03-31 US US15/301,251 patent/US10800918B2/en active Active
  • 2015-03-31 CN CN201580017644.4A patent/CN106133061B/zh active Active
• 2019
  • 2019-09-12 JP JP2019165874A patent/JP2020007563A/ja active Pending

Patent Citations (1)

Non-Patent Citations (1)

Also Published As

Similar Documents

Legal Events