• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to a tubular structure for transporting heat transfer fluid, in particular refrigerant fluid, comprising at least: i) a layer (1) in contact with the fluid comprising at least one semi-thermoplastic polymer Pi crystalline of Tfi greater than or equal to 160 ° C, in particular greater than or equal to 170 ° C as determined according to standard 11357-3 (2013) or amorphous of Tgi greater than or equal to 100 ° C, preferably 120 ° C in particular 140 ° C as determined according to standard 11357-2 (2013), said layer (1) being free of fibers, ii) a layer (2) comprising at least: (a) a semicrystalline thermoplastic polymer P2, in particular a polyamide of Tf2 greater than or equal to 170 ° C or amorphous of Tg2 greater than or equal to 100 ° C, or a polyolefin of Tf greater than 100 ° C; (b) continuous fibers, the polymer P2 being identical to Pi or different from Pi in which case the polymers P1 and P2 adhere at least partially to each other.
    公开号:FR3044959A1
    申请号:FR1562378
    申请日:2015-12-15
    公开日:2017-06-16
    发明作者:Benoit Brule；Nicolas Dufaure；Pierrat Estelle Meurice
    申请人:Arkema France SA；
    IPC主号:
    专利说明:

    MULTILAYER STRUCTURE COMPRISING CONTINUOUS FIBERS FOR TRANSPORTING HEAT TRANSFER FLUID
    FIELD OF THE INVENTION
    The present invention relates to a multilayer tubular structure comprising at least one inner layer and a second layer comprising in particular continuous fibers. The invention also relates to the use of this structure for transporting heat transfer fluid, in particular refrigerant such as R134, R-1234yf or R-1234ze, in particular in the field of automotive air conditioning.
    TECHNICAL BACKGROUND
    The transport of heat transfer fluid, in particular refrigerant in vapor compression circuits, such as those used in particular in automotive air conditioning, requires the use of multilayer structures having a set of mechanical properties, thermal, and specific chemicals.
    The elements of these circuits (and in particular multilayer tubular structures) must in particular: - be sealed to the fluids transported and therefore have barrier properties with respect to these fluids (and in particular fluorocarbon refrigerant compounds such as R134, R -1234yf or R-1234ze), as well as water and oxygen; - have chemical resistance to transported fluids, as well as compressor oils, water and oxygen, in order to avoid excessive degradation over the long term; - have a sufficient mechanical strength (in particular resistance to bursting) but also sufficient flexibility in the case where the two ends of the tube are connected to parts that can move relative to each other (in particular in the automotive air conditioning, where the constraints of space and mounting under the bonnet impose to bend the tubular structures) and allow vibration damping; - have a satisfactory thermal resistance, considering that the fluids transported can be at a high temperature, and that the temperature of the environment can also be high (in particular in the car air-conditioning, the parts concerned being able to be arranged in the vicinity of the motor). At present, tubular structures for transporting heat transfer fluids and in particular refrigerants in automotive air conditioning include rigid metal portions (usually aluminum) and flexible portions in multilayer tubes. Some of these multilayer tubes are known under the English name of "veneer" tubes; they comprise successively, from the inside towards the outside, a barrier inner layer based on polyamide (or PA), an intermediate layer of rubber-type elastomer, a reinforcement braid and finally another layer of elastomer-type rubber.
    In commercially available models, the polyamide-based inner layer may be, for example, a PA 6 (polycaprolactam) formulated (with or without a plasticizer, with or without an impact modifier, with or without a stabilizer), a PA 6/66 copolyamide. formulated (with or without a plasticizer, with or without an impact modifier, with or without a stabilizer), or an alloy of PA 6 or PA 66 (polyhexamethylene adipamide) with functionalized polyolefins and polyolefins (product marketed under the trade name Orgalloy®) .
    Furthermore, the document US 2011/0183095 describes a tube or a seal for transporting heat transfer fluids in automotive air conditioning, comprising an inner layer based on PA 610 (polyhexamethylene sebacamide) and an outer layer based on a polyamide such as a polyphthalamide and preferably the seal is composed of PA 610 reinforced with fibers.
    US 2011/0272854 discloses an article comprising a fiber-reinforced polyamide member overmolded with another polyamide member optionally with a binder between the two members and wherein at least one of the polyamides is a semi-aromatic polyamide. .
    EP 1717022 relates to multilayer pipes for various applications, and more particularly for the transport of fuel in vehicles, from the tank to the engine. These tubes comprise an intermediate layer of polyamide, for example PA 610 (polyhexamethylene sebacamide) or PA 612 (polyhexamethylene dodecanamide).
    WO 2014/125218 relates to the use of a layer consisting of a composition comprising a copolyamide of formula X / 10T / Y for the transport of a heat transfer fluid in a vapor compression circuit.
    The document WO 2014/125219 relates to a thermoplastic structure comprising at least one layer consisting of a composition based on semi-aromatic copolyamide. The thermoplastic structure is particularly suitable for carrying heat transfer fluid transport (such as R-1234yf), in particular in the field of automotive air conditioning.
    There is a need to develop vapor compression circuit elements and therefore tubular structures for transporting transfer fluid, in particular refrigerant such as R-1234yf or R-1234ze, which make it possible to satisfy the specifications of the invention. loads in terms of sealing properties of transported fluids (and in particular refrigerants such as R-1234yf or R-1234ze), as well as water and oxygen, chemical resistance to transported fluids as well as compressor oils, water and oxygen, mechanical properties, possibly flexibility, thermal resistance and especially to simplify and lighten these multilayer structures.
    Indeed, the need for relief is particularly felt in the field of automotive air conditioning, particularly when the heat transfer fluid is R-1234yf or R-1234ze, since it is to improve the overall environmental impact of the vehicle that is to say that of the content of the heat transfer fluid but more generally the container that is to say the vehicle and therefore the structure leading the heat transfer fluid .
    There is also a need for simplification of implementation of vapor compression circuit elements, especially in automotive air conditioning.
    SUMMARY OF THE INVENTION The invention relates primarily to a tubular structure (all or part of the system) for transporting heat transfer fluid, in particular refrigerant comprising at least i) a layer (1) in contact with the fluid comprising at least one semi-crystalline thermoplastic polymer Pi of greater than or equal to 160 ° C, in particular greater than or equal to 170 ° C as determined according to standard 11357-3 (2013) or amorphous Tgi greater than or equal to 100 ° C, preferably 120 ° C in particular 140 ° C as determined according to standard 11357-2 (2013), said layer (1) being free of fibers, ii) a layer (2) comprising at least (a) a semicrystalline thermoplastic polymer P2, in particular a Tf2 polyamide greater than or equal to 170 ° C or amorphous of Tg2 greater than or equal to 100 ° C or a polyolefin of Tf greater than 100 ° C; (b) continuous fibers, the polymer P2 being identical to Pi or different from Pi in which case the polymers Pi and P2 adhere at least partially to each other.
    An amorphous polyamide, within the meaning of the invention, denotes a polyamide having only a glass transition temperature (no melting temperature (Tf)), or a very low crystallinity polyamide having a glass transition temperature and a melting point such as that the enthalpy of crystallization during the cooling step at a speed of 20K / min in Differential Scanning Calorimetry (DSC) measured according to the ISO 11357-3 standard of 2013 is less than 30 J / g, especially less than 20 J / g, preferably less than 15 J / g. The glass transition temperature (Tg) measured by DSC at a heating rate of 20K / min according to the ISO 11357-2 standard of 2013 for these polyamides is greater than 75 ° C.
    A semicrystalline polyamide, within the meaning of the invention, denotes a polyamide which has a melting point (Tf) in DSC according to the ISO 11357-3 standard of 2013, and a crystallization enthalpy during the cooling stage at a speed of 20K / min in DSC measured according to the ISO 11357-3 standard of 2013 greater than 30 J / g, preferably greater than 40 J / g. The term "fiber-free" means that the P1 layer does not include short, long or continuous fibers, whether mineral fibers, polymeric fibers or polymer, or mixtures of the aforementioned fibers. The expression "Pi and P2 adhere at least partially to each other" means that Pi and P2 are at least partially directly and firmly bonded together without the presence of an adhesive between the two or another layer.
    It also means that there is no layer of binder or braid, whatever its composition, between the two layers (1) and (2).
    According to one embodiment, said polymer Pi is chosen from polyamides and EVOH, in particular polyamides.
    According to one embodiment, the polymer Pi is a semi-crystalline polyamide.
    According to one embodiment, the polymer P2 is chosen from polyamides and polyolefins.
    According to one embodiment, the polymer P2 is a semi-crystalline polyamide.
    According to one embodiment, said polymer Pi is a semi-crystalline polyamide and said polymer P2 is chosen from polyamides and polyolefins.
    According to one embodiment, said polymer Pi is chosen from polyamides and EVOH, in particular polyamides, and polymer P2 is a semi-crystalline polyamide.
    According to one embodiment, said polymer Pi is chosen from polyamides and EVOH, in particular polyamides, and said polymer P2 is chosen from polyamides and polyolefins.
    According to one embodiment, the polymers Pi and P2 are semi-crystalline polyamides.
    According to one embodiment, the polymer P2 is an amorphous polyamide.
    According to one embodiment, the polymer Pi is a semi-crystalline polyamide and the polymer P2 is an amorphous polyamide.
    According to one embodiment, the polymer Pi is an amorphous polyamide and the polymer P2 is a semi-crystalline polyamide.
    Advantageously, the polymer Pi of the various embodiments above is a polyamide chosen from polyphthalamides, semi-aromatic polyamides, in particular A / T, A / 10T, A / 6T, XY / 10T, XY / 6T, PA6. PA66, PA6 / 66, PA610, PA612, a short chain C4-C8 polyamide, especially derived from the polymerization of lactams or C4-C8 aminocarboxylic acids, or the polymerization of at least one diamine and at least one acid dicarboxylic whose average number of carbon atoms is between C4 and C8, and a PA / polyolefin mixture, said polyolefin may be functionalized (in whole or in part) or not, in particular an Orgalloy®. A being a unit derived from the polycondensation of a lactam or a C6 to C12 amino acid. X corresponding to a unit derived from the polycondensation of an aliphatic, cycloaliphatic or aromatic diamine with an aliphatic, cycloaliphatic or aromatic dicarboxylic acid.
    Advantageously, the polymer Pi of the various embodiments above is a polyamide chosen from polyphthalamides, semi-aromatic polyamides, in particular 11 / 1OT, 612 / 10T, 11 / 6T, PA6, PA66, PA6 / 66, PA610. PA612, a C4-C8 short chain polyamide, especially derived from the polymerization of lactams or C4-C8 aminocarboxylic acids, or the polymerization of at least one diamine and at least one dicarboxylic acid whose average number of atoms carbon is comprised from C4 to C8, and a PA / polyolefin mixture, said polyolefin may be functionalized (in whole or in part) or not, in particular an Orgalloy®.
    Advantageously, the polymer Pi of the various embodiments above is a polyamide chosen from semi-aromatic polyamides, in particular 11 / 1OT, 612 / 10T, 11 / 6T, PA6, PA66, PA6 / 66, PA610, PA612, a a C4 to C8 short chain polyamide, in particular resulting from the polymerization of lactams or C4-C8 aminocarboxylic acids, or the polymerization of at least one diamine and at least one dicarboxylic acid whose average number of carbon atoms is from C4 to C8, and a PA / polyolefin mixture, said polyolefin may be functionalized (in whole or in part) or not, in particular an Orgalloy®.
    Advantageously, the polymer P2 of the various embodiments above is a polyamide, in particular chosen from polyphthalamides, semi-aromatic polyamides, in particular 11 / 10T and 11 / 6T, PA11, PA12, PA6, PA66, PA6 / 66, PA610, PA612.
    Advantageously, in the various embodiments above, the polymer Pi is chosen from a polyphthalamide, a semi-aromatic polyamide, in particular 11/1 OT, 612/10T, 11 / 6T, PA6, PA66, PA6 / 66, PA610. , PA612, a C4-C8 short chain polyamide, especially derived from the polymerization of lactams or C4-C8 aminocarboxylic acids, or from the polymerization of at least one diamine and at least one dicarboxylic acid whose average number of carbon atom is comprised of C4 to C8, and a PA / polyolefin mixture, said polyolefin may be functionalized (all or part) or not, in particular an Orgalloy® and the polymer P2 is a polyamide, in particular chosen from polyphthalamides, semi-aromatic polyamides, especially 11 / 10T and 11 / 6T, PA11, PA12, PA6, PA66, PA6 / 66, PA610, PA612.
    Advantageously, in the various embodiments above, the polymer Pi is chosen from a polyphthalamide, a semi-aromatic polyamide, in particular 11/1 OT, 612/1 OT, 11 / 6T, PA6, PA66, PA6 / 66, a C4-C8 short chain polyamide, especially derived from the polymerization of lactams or C4-C8 aminocarboxylic acids, or from the polymerization of at least one diamine and at least one dicarboxylic acid whose average number of carbon atoms is comprised of C4 to C8, and a PA / polyolefin mixture, said polyolefin may be functionalized (all or part) or not, in particular an Orgalloy®, excluding PA610 and PA612.
    Advantageously, in the various embodiments above, the polymer Pi is chosen from a semi-aromatic polyamide, in particular 11 / 10T, 612 / 10T, 11 / 6T, PA6, PA66, PA6 / 66, a short-chain polyamide C4 to C8, in particular resulting from the polymerization of lactams or C4-C8 aminocarboxylic acids, or from the polymerization of at least one diamine and at least one dicarboxylic acid, the average number of carbon atoms of which is from C4 to C8, and a PA / polyolefin mixture, said polyolefin may be functionalized (all or part) or not, in particular an Orgalloy®, excluding PA610 and PA612.
    Advantageously, in the various embodiments above, the polymer Pi and / or said polymer P2 comprises at least one binder.
    Said binder is mixed with either Pi, P2 or Pi and P2 but does not constitute a binder layer between Pi and P2.
    It is possible to use the binders described in EP 2098365 and EP 2098580, which are expressly referred to herein.
    In summary, the binders in question are compositions comprising at least one polyamide noted A having an average number of carbon atoms per nitrogen atom noted Ca ranging from 4 to 8.5, advantageously from 4 to 7; at least one polyamide noted B having a melting point greater than or equal to 180 ° C and an average number of carbon atoms per nitrogen atom Cb of 7 to 10, preferably 7.5 to 9.5; and at least one C-noted polyamide having an average number of carbon atoms per nitrogen atom of C 9 to 18, preferably 10 to 18; at least 50% by weight of said composition being formed of one or more polyamides chosen from polyamides A, B and C, the mass-weighted average of the melting enthalpies of these polyamides within said composition being greater than 25 J / g (measured by DSC), and the average number of carbon atoms per nitrogen atom of the polyamides A, B and C further meeting the following strict inequality: Ca <Cb <Ce.
    The difference between the average numbers of carbon atoms per nitrogen atom (Cb-Ca) and / or (Cc-Cb) is advantageously from 1 to 4, and preferably from 2 to 3.
    Each of the polyamides A, B and C preferably has a melting enthalpy greater than 25 J / g (measured by DSC).
    The binder is used as an additive in a layer of non-adhesive material.
    According to one embodiment, the structure, defined in one of the embodiments above, comprises at least a third outer layer (3), said layer being in contact with the layer (2) and comprising an elastomer and / or a polymer P3 identical to or different from Pi and adhering at least partially to P2. The expression "adhering at least partially" has the same meaning as above.
    Advantageously, the continuous fibers used in the above embodiments are chosen from: - mineral fibers, - carbon fibers or carbon nanotubes, - polymeric or polymer fibers, - or mixtures of the aforementioned fibers.
    Advantageously, the mineral fibers are chosen from: silica fibers such as glass fibers, in particular of type E, R or S2; boron fibers; ceramic fibers, especially silicon carbide, boron carbide, boron carbonitride, silicon nitride, boron nitride; basalt fibers; fibers or filaments based on metals and their alloys; fibers based on metal oxides; metallized carbon fibers and metallized glass fibers or mixtures of the fibers mentioned.
    Advantageously, the polymeric fibers are chosen from: thermosetting polymer fibers thermoplastic polymer fibers polyamide fibers corresponding to one of the following polyamides: 6, 66, 610, 612, 46, 410, 1010, 1012, 11 and 12
    aramid fibers and aromatic polyamides such as those corresponding to one of the formulas: PPD.T, MPD.I, PAA and PPA or the aforementioned fiber mixtures.
    Advantageously, the proportion by weight of fibers in P2 is from 30 to 80%, preferably from 50 to 70%.
    Advantageously, the continuous fibers are glass fibers.
    The glass fibers may or may not be sized, i.e., for example, the glass fibers are sized by a solution containing an alkoxysilane. It may be, for example, glass fibers treated by sizing with the same solution as that described in document JP H1 139628.
    Advantageously, the refrigerant used in one of the above embodiments is chosen from hydrocarbons, hydrofluorocarbons, ethers, hydrofluoroethers or fluoroolefins, in particular from fluoropropenes, fluoropropanes and fluoroethanes; preferably from 1,3,3,3-tetrafluoropropene, 2,3,3,3-tetrafluoropropene, 1,2,3,3,3-pentafluoropropene, 1,1,3,3-tetrafluoropropene, 3,3, 3-trifluoropropene, 2,3,3-trifluoropropene, 1,1,1,2-tetrafluoroethane, 1,1,2,2-tetrafluoroethane, pentafluoroethane, difluoromethane, 1,1-difluoroethane, , 1,1,1,3,3,3-heptafluoropropane, 1,1,1-trifluoropropane, 1,1,1,3,3,3-hexafluoropropane, 1,1,1,3,3-pentafluoropropane, 1,1,3,3-pentafluorobutane, trifluoroiodomethane and mixtures thereof; and particularly preferably said refrigerant being 2,3,3,3-tetrafluoropropene (1234yf) or 1,3,3,3-tetrafluoropropene (1234ze).
    Advantageously, the refrigerant is added with a lubricant, preferably selected from mineral oils, silicone oils, paraffins of natural origin, naphthenes, synthetic paraffins, alkylbenzenes, poly-alpha olefins, polyalkylene glycols, polyol esters and / or polyvinyl ethers; the lubricant is more preferably a polyalkylene glycol or a polyol ester.
    Advantageously, the lubricant is in proportion by weight of 0.5 to 50%, in particular of 1 to 15% by weight.
    According to one embodiment, the structure is a vapor compression circuit element for containing or transporting a refrigerant.
    Steam compression circuit element
    The composition of the invention described above is used as a layer in a vapor compression circuit element.
    A vapor compression circuit includes at least one evaporator, a compressor, a condenser and an expander, and heat transfer fluid transport lines between these elements. The evaporator and the condenser comprise a heat exchanger for heat exchange between a heat transfer fluid circulating in the circuit and another fluid or body. The facility may include a turbine to generate electricity (Rankine cycle).
    The vapor compression circuit may be integrated in an installation which may also optionally include at least one coolant circuit used to transmit heat (with or without a change of state) between the heat transfer fluid circuit and the fluid. or body to be heated or cooled. The installation may also optionally include two or more vapor compression circuits containing identical or different heat transfer fluids. For example, the vapor compression circuits may be coupled together.
    The vapor compression circuit operates in a conventional vapor compression cycle. The cycle comprises changing the state of the heat transfer fluid from a liquid phase (or two-phase liquid / vapor) to a vapor phase at a relatively low pressure, and then compressing the fluid in the vapor phase to a relatively high pressure. high, the change of state (condensation) of the heat transfer fluid from the vapor phase to the liquid phase at a relatively high pressure, and the reduction of the pressure to restart the cycle.
    In the case of a cooling process, heat from the fluid or the body that is cooled (directly or indirectly, via a coolant) is absorbed by the heat transfer fluid, during the evaporation of the latter, and this at a relatively low temperature compared to the environment. Cooling processes include air conditioning processes (with mobile installations, for example in vehicles, or stationary), refrigeration (with mobile installations for example in containers, or stationary) and freezing or cryogenics.
    In the case of a heating process, heat is transferred (directly or indirectly via a heat transfer fluid) from the heat transfer fluid, during the condensation thereof, to the fluid or to the body that is heating, and this at a relatively high temperature compared to the environment. The installation for implementing the heat transfer is called in this case "heat pump".
    By "vapor compression circuit element" is meant according to the present invention any piece of such a circuit, having a light, said part being adapted to contain or transport the heat transfer fluid. The vapor compression circuit element which is the subject of the present invention is preferably a pipe or tubing (or a hose). Alternatively, it may be a connector or connector between tubings, or between tubing and compressor, or condenser, or heat exchanger, or a portion of a buffer capacity or a heat exchanger. The term "light" refers to the interior of said part of said circuit, in particular the inside of the pipe or tubing or the inside of the fitting or connector. The vapor compression circuit element may also be a heat exchanger as such (in which case it comprises at least two lumens for the circulation of two identical or different fluids, one to yield heat to the other).
    The heat transfer fluid may be contained or transported in gaseous, liquid or two-phase form in the above circuit element.
    The composition layer according to the invention described above may in particular be a monolayer, or be an inner layer (intended to come into contact with the heat transfer fluid) or an outer layer (intended to be in contact with the environment ) of the circuit element. It is preferred that this layer constitutes an inner layer (or coating). The subject of the invention is also a process for manufacturing the structure as described above, comprising at least one stage of extrusion of the layer
    (U
    According to one embodiment, the manufacturing method of the structure as described above comprises the following successive steps: a. manufacturing said layer (1) by extrusion through an annular die and b. depositing on said layer (1) of said outer layer (2) in the molten state by the filament winding technique of polymer impregnated fibers P2 in the molten state with one or more angles of orientation relative to the axis of said structure and c. cooling said structure. The invention also relates to the use of a structure as described above for the transport of a refrigerant in a vapor compression circuit, particularly R-1234yf or R-1234ze.
    The present invention makes it possible to overcome the drawbacks of the state of the art in that it provides a structure which makes it possible to satisfy the specifications in terms of sealing properties for the fluids transported (and in particular for refrigerants such as the R-1234yf or R-1234ze), as well as water and oxygen, chemical resistance to transported fluids, as well as water and oxygen, mechanical properties, flexibility, thermal resistance but especially to simplify the structures used in terms of number of layers and implementation and lighten these multilayer structures, and easier to implement, lighter and therefore lower environmental impact.
    Compared to the multilayer structures which are used today commercially as components of automobile air-conditioning vapor compression circuits, the structures of the invention exhibit, in particular, improved properties, enabling them to be used as a layer with improved properties: heat transfer fluids (especially R-1234yf or R-1234ze, but also R-134a for example); and / or - dimensional stability with water; and / or - water barrier; and / or - thermal and chemical resistance in the presence of R-1234yf or R-1234ze and lubricant, in particular of the PAG type; and / or - long term heat resistance; and / or - flexibility in the case where the two ends of the tube are connected to parts that can move relative to each other.
    Furthermore, the realization of these structures with layers of polymers, compared to traditional rubber structures with an inner layer of polyamide, connected to aluminum structures, simplifies the connections and limit the risk of leakage.
    It also allows a reduction of weight of the structures and a reduction of cost.
    The Tg and the Tf are conventionally measured by DSC (differential scanning calorimetry) according to the standard 11357-2 (2013) and the standard 11357-3 (2013), respectively. They are determined here during a temperature ramp of 20 ° C / min.
    As will be detailed below, the structure may comprise one or more polymers, organized in two or more layers. It may also comprise various additives and fillers (and in particular one or more elastomeric polymers mixed with the thermoplastic polymers and not affecting the thermoplastic nature of the compositions concerned).
    The additives or fillers are different from the fibers.
    DESCRIPTION OF EMBODIMENTS OF THE INVENTION The invention is now described in more detail and in a nonlimiting manner in the description which follows.
    The thermoplastic polymer P1 or P2 With regard to the thermoplastic polymer, it can be semi-crystalline or amorphous.
    When the thermoplastic polymer is P1, it is chosen from polyamides and EVOH, in particular it is a polyamide or a mixture of polyamides.
    When the thermoplastic polymer is P2, it is chosen from polyamides and polyolefins. With regard to polyamides or mixtures of polyamides.
    The nomenclature used to define polyamides is described in ISO 1874-1: 1992 "Plastics - Polyamides (PA) for molding and extrusion - Part 1: Designation", in particular on page 3 (Tables 1 and 2) and is well known to those skilled in the art.
    The polyamide according to the present invention may have a homopolyamide or copolyamide structure.
    By homopolyamide, within the meaning of the present invention, is meant a polyamide, which consists only of the repetition of a single unit.
    For the purposes of the present invention, the term "copolyamide" means a polyamide, which consists of the repetition of at least two units of different chemical structure. This copolyamide may have a random, alternating or block structure.
    The polyamide according to the present invention may comprise one or more structural units selected from amino acids, lactams and (diamine) units (diacid).
    When the polyamide has an amino acid in its structure, it may be chosen from 9-aminononanoic acid (A = 9), 10-aminodecanoic acid (A = 10) and 10-aminoundecanoic acid (A = 11). , 12-aminododecanoic acid (A = 12) and 11-aminoundecanoic acid (A = 11) and its derivatives, especially N-heptyl-11-aminoundecanoic acid, A denoting the number of carbon atoms in the pattern.
    When the polyamide comprises a lactam, it may be chosen from pyrrolidinone, 2-piperidinone, caprolactam, enantholactam, caprylolactam, pelargolactam, decanolactam, undecanolactam, and lauryllactam (A = 12).
    When the polyamide contains is a unit corresponding to the formula (diamine in Ca). (Diacid in Cb) Ca and Cb designating the number of carbon atoms respectively in the diamine and the diacid, the unit (diamine in Ca) is chosen among the linear or branched aliphatic diamines, cycloaliphatic diamines and alkylaromatic diamines.
    When the diamine is aliphatic and linear, of formula H2N- (CH2) a-NH2, the monomer (diamine Ca) is preferably selected from butanediamine (a = 4), pentanediamine (a = 5), hexanediamine ( a = 6), heptanediamine (a = 7), octanediamine (a = 8), nonanediamine (a = 9), decanediamine (a = 10), undecanediamine (a = 11), dodecanediamine (a = 12), tridecanediamine (a = 13), tetradecanediamine (a = 14), hexadecanediamine (a = 16), octadecanediamine (a = 18), octadecenediamine (a = 18), eicosanediamine (a = 20), docosanediamine (a = 22) and diamines obtained from fatty acids.
    When the diamine is aliphatic and branched, it may have one or more methyl or ethyl substituents on the main chain. For example, the monomer (Ca-diamine) may advantageously be chosen from 2,2,4-trimethyl-1,6-hexanediamine, 2,4,4-trimethyl-1,6-hexanediamine, 1,3-trimethyl-1,6-hexanediamine and diaminopentane, 2-methyl-1,5-pentanediamine, 2-methyl-1,8-octanediamine.
    When the monomer (diamine in Ca) is cycloaliphatic, it is chosen from bis (3,5-dialkyl-4-aminocyclohexyl) methane, bis (3,5-dialkyl-4-aminocyclohexyl) ethane, bis (3, 5-dialkyl-4-aminocyclohexyl) propane, bis (3,5-dialkyl-4-aminocyclohexyl) butane, bis- (3-methyl-4-aminocyclohexyl) methane (BMACM or MACM), p-bis (aminocyclohexyl) methane (PACM) and isopropylidenedi (cyclohexylamine) (PACP), isophoronediamine (a = 10), piperazine (a = 4), amino-ethylpiperazine. It may also comprise the following carbon skeletons: norbornyl methane, cyclohexylmethane, dicyclohexylpropane, di (methylcyclohexyl), di (methylcyclohexyl) propane. A non-exhaustive list of these cycloaliphatic diamines is given in the publication "Cycloaliphatic Amines" (Encyclopaedia of Chemical Technology, Kirk-Othmer, 4th Edition (1992), pp. 386-405).
    When the monomer (Ca diamine) is alkylaromatic, it is chosen from 1,3-xylylene diamine and 1,4-xylylenediamine.
    The (Cb diacid) unit is chosen from linear or branched aliphatic diacids, cycloaliphatic diacids and aromatic diacids.
    When the monomer (diacid Cb) is aliphatic and linear, it is selected from succinic acid (b = 4), pentanedioic acid (b = 5), adipic acid (b = 6), acid heptanedioic acid (b = 7), octanedioic acid (b = 8), azelaic acid (b = 9), sebacic acid (b = 10), undecanedioic acid (b = 11), acid dodecanedioic acid (b = 12), brassylic acid (b = 13), tetradecanedioic acid (b = 14), hexadecanedioic acid (b = 16), octadecanedioic acid (b = 18), acid octadecenedioic acid (b = 18), eicosanedioic acid (b = 20), docosanedioic acid (b = 22) and fatty acid dimers containing 36 carbons.
    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.
    When the diacid is cycloaliphatic, it may comprise the following carbon skeletons: norbornyl methane, cyclohexylmethane, dicyclohexylmethane, dicyclohexylpropane, di (methylcyclohexyl), di (methylcyclohexyl) propane.
    When the diacid is aromatic, it is selected from terephthalic acid (noted T), isophthalic acid (noted I) and naphthalenic diacids.
    Advantageously, the proportion of polyamide Pi is at least 55% by weight.
    Advantageously, the proportion of polyamide P2 is from 10 to 70% by weight, especially from 20 to 50% by weight, preferably from 30 to 40% by weight.
    Advantageously, the proportion of polyamide Pi is at least 55% by weight and the proportion of polyamide P2 is 20 to 50% by weight, preferably 30 to 40% by weight.
    Advantageously, the proportion of polyamide Pi is at least 55% by weight and the proportion of polyamide P2 is 10 to 70% by weight, especially 20 to 50% by weight, preferably 30 to 40% by weight. weight and the proportion of fibers in P2 is from 30% to 80% by weight, especially from 30 to 50% by weight.
    Advantageously, said polyamide Pi is as defined above.
    Advantageously, said P2 polyamide is as defined above.
    Advantageously, Pi and P2 are identical.
    The polyamide of the invention advantageously has a polymolecularity index, denoted Ip of less than or equal to 3.5. Preferably, the polymolecularity index of said polyamide is from 2.0 to 3.0.
    This index is measured in a conventional manner and known to those skilled in the art, by steric exclusion chromatography or gel permeation. Preferably, the polymolecularity index of the polyamides of the invention is measured by gel permeation chromatography. More particularly, it is measured in a suitable solvent for the polyamide, such as a fluorinated solvent such as hexafluoroisopropanol, at a temperature of 20 ° C to 50 ° C, preferably at 40 ° C.
    If most of the monomers or starting materials contemplated in the present description (amino acids, diamines, diacids) are saturated, there is no reason to consider that they may be partially unsaturated.
    It will be noted, for example, that the C18 dicarboxylic acid may be octadecanedioic acid, which is saturated, or octadecenedioic acid, which, for its part, exhibits unsaturation.
    The polyamide of the invention may comprise monomers derived from resources derived from renewable raw materials, that is to say comprising organic carbon derived from biomass and determined according to the ASTM D6866 standard. These monomers derived from renewable raw materials may be 1,10-decanediamine or, when present, in particular 11-aminoundecanoic acid, diamines and aliphatic and linear diacids as defined above.
    The polyamides of the invention may be prepared by polycondensation of the comonomers defined above, for example in the presence of hypophosphorous acid or at least one of its salts.
    The detailed description of such a polycondensation process can be found in document WO 2010/015786.
    The polyamide of the invention preferably has an amino chain end content of 20 mmol / kg or greater, an acid chain end content of 100 mmol / kg or less, and a non-reactive chain end content. greater than or equal to 20 mmol / kg.
    The end-of-chain content of each of the amine, acid and non-reactive function functions is conventionally measured by NMR (Nuclear Magnetic Resonance).
    In order to adjust the end-of-chain content, it is possible to use chain terminating agents, that is compounds capable of reacting with the amine and / or carboxylic acid terminal functions of the polyamides, stopping thus the reactivity of the end of the macromolecule, and thus the polycondensation.
    Suitable chain terminators for reacting with the terminal amine function may be monocarboxylic acids, anhydrides, such as phthalic anhydride, monohalogen acids, monoesters or monoisocyanates. Preferably, the monocarboxylic acids are used. They may be chosen from aliphatic monocarboxylic acids, such as acetic acid, propionic acid, lactic acid, valeric acid, caproic acid, capric acid, uric acid, tridecyl acid, myristic acid, palmitic acid, stearic acid, pivalic acid and isobutyric acid; alicyclic acids, such as cyclohexanecarboxylic acid; monocarboxylic aromatic acids such as toluic acid, α-naphthalenecarboxylic acid, β-naphthalenecarboxylic acid, methylnaphthalene carboxylic acid, phenylacetic acid; and their mixtures. The preferred compounds are aliphatic acids, in particular acetic acid, propionic acid, lactic acid, valeric acid, caproic acid, capric acid, lauric acid and tridecyl acid. myristic acid, palmitic acid and stearic acid.
    Among the chain terminating agents suitable for reacting with the acid terminal function, monoamines, monoalcohols, monoisocyanates may be mentioned. Preferably, the monoamines are used. They may be chosen from aliphatic monoamines, such as methylamine, ethylamine, propylamine, butylamine, hexylamine, octylamine, decylamine, laurylamine, stearylamine, dimethylamine, diethylamine and dipropylamine. dibutylamine; alicyclic amines, such as cyclohexylamine and dicyclohexylamine; aromatic monoamines, such as aniline, toluidine, diphenylamine and naphthylamine; and their mixtures.
    The preferred compounds are butylamine, hexylamine, octylamine, decylamine, laurylamine, stearylamine, cyclohexylamine and aniline.
    It is also possible to react the acid and / or amine ends respectively with mineral bases such as alkali and alkaline earth hydroxides such as potassium hydroxide and sodium hydroxide, and with mineral acids such as HCl, HNO 3 and H 2 SO 4.
    The chain terminators may be introduced during the first and / or second stage, in the case of the two-step manufacturing processes described above. Reference is made here for more details to WO 2010/015785. With regard to polyolefins
    The polyolefin may be functionalized or non-functionalized or be a mixture of at least one functionalized and / or at least one non-functionalized, with a Tf greater than 100 ° C.
    By polyolefin is meant a homopolymer or copolymer comprising one or more olefin units such as ethylene, propylene, butene-1, octene-1, butadiene, or any other alpha-olefin units. As an example of a polyolefin, mention may be made of polyethylene and, in particular, low density polyethylene (LDPE), high density polyethylene (HDPE), linear low density polyethylene (LLDPE) and very low density polyethylene (VLDPE). ); polypropylene; ethylene / propylene copolymers; or the metallocene polyethylenes obtained by monosite catalysis.
    Copolymers of ethylene and EVA (with a Tf greater than 100 ° C.) are also preferred.
    additives
    It is possible to add to the polyamide P1 and / or P2 and to the polyolefin, at the end of its manufacturing process, besides the diamine balance, usual additives, as defined below, depending on the layer in which they are present:
    Polymer P1
    The polymer Pi may comprise at least one additive selected from an antioxidant, a thermal stabilizer, a UV absorber, a light stabilizer, a lubricant, a filler, a flame retardant, a nucleating agent, a plasticizer, a shock modifier and a dye.
    Fibers are excluded from the additives and in particular the term "filler" excludes fibers.
    Preferably, the additives of the polyamide Pi of the invention are present in an amount of 1 to 45%, preferably 5 to 45%, or 15 to 45%, by weight relative to the weight of the composition present in P1. .
    By the term "impact modifier" is meant a polyolefin-based polymer having a flexural modulus of less than 100 MPa measured according to ISO 178: 2010 and a Tg of less than 0 ° C (measured according to standard 11357-2). : 2013 at the inflection point of the DSC thermogram).
    The polyolefin may be functionalized or not.
    When the polyolefin is functionalized, 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 character (EPR), a ethylene-propylene-diene copolymer with elastomeric character (EPDM) and an ethylene / alkyl (meth) acrylate copolymer, an ethylene-higher alkene copolymer, in particular an ethylene-octene copolymer, an ethylene-alkyl acrylate-anhydride terpolymer maleic.
    The plasticizer used as additive in the polymer Pi is advantageously a plasticizer which has good thermal stability so that no smoke is formed during the mixing steps of the various polymers and transformation of the composition obtained.
    In particular, this plasticizer may be chosen from: benzene sulphonamide derivatives such as n-butyl benzene sulphonamide (BBSA), ortho and para isomers of ethyl toluene sulphonamide (ETSA), N-cyclohexyl toluene sulphonamide and N- (2-hydroxypropyl) benzenesulfonamide (HP-BSA), - esters of hydroxybenzoic acids such as 2-ethylhexyl para-hydroxybenzoate (EHPB) and decyl-2-hexyl para-hydroxybenzoate (HDPB), the esters or ethers of tetrahydrofurfurylalcohol such as oligoethyleneoxy-tetrahydrofurfurylalcohol, and the esters of citric acid or of hydroxymalonic acid, such as oligoethyleneoxymalonate.
    A preferred plasticizer, because commonly used, is n-butyl benzene sulfonamide (BBSA).
    It is also possible to use a mixture of plasticizers.
    The plasticizer used as additive in the polymer Pi is in a mass proportion of 0 to 15%, more particularly preferably 0 to 8%.
    Advantageously, the polymer Pi comprises a shock modifier and a plasticizer.
    The thermal stabilizer used as additive in the polymer Pi can be present in an amount of 0 to 4%, especially 0.01 to 2% or 0.1 to 1% by weight relative to the total weight of the polymer composition. ft.
    It can be an organic or copper thermal stabilizer.
    More particularly, it may be a copper salt or a copper salt derivative, for example copper iodide, copper bromide, copper halides, derivatives or mixtures thereof. -this. The copper salts I are preferred. Examples are copper iodide, copper bromide, copper chloride, copper fluoride, copper thiocyanate, copper nitrate, copper acetate, copper naphthenate, copper caprate, copper laurate, copper stearate, copper acetylacetonate, copper oxide. Copper iodide, copper bromide, copper chloride, copper fluoride are preferred.
    It is also possible to provide as a thermal stabilizer a metal halide salt in combination with Lil, Nal, Kl, Mgh, KBr or Cah. K1 and KBr are preferred. Other possible heat stabilizers are hindered phenolic antioxidants. These compounds are described in detail in US 2012/0279605, paragraphs [0025] and [0026], which are expressly referred to herein.
    However, according to an alternative embodiment, the composition of the invention is devoid of such hindered phenolic antioxidants.
    A secondary phosphite antioxidant can also be used.
    Another class of possible stabilizers are sterically hindered amine UV stabilizers (or HALS), which are derivatives of 2,2,6,6-tetramethylpiperidine. They can be used for example in a range of 0 to 1%, or 0.01 to 0.5%.
    Among the dyes, mention may in particular be made of carbon black. The dyes or pigments (for the purpose of coloring the composition) may be present, for example, in an amount of 0.1 to 0.2% by weight.
    Among the fillers, mention may be made of silica, graphite, expanded graphite, carbon black, glass beads, kaolin, magnesia, slag, talc, metal oxides (titanium oxide), metals.
    Expenses such as expanded graphite, for example, may make it possible to increase the thermal conductivity of the material (for example in order to promote a heat exchange between a light of a tube comprising a composition layer of the invention and the outside, or between two lumens of a tube comprising a composition layer of the invention).
    Polymer P2
    The polymer P2 can comprise: additives absorbing in the UV or IR so as to allow the welding of the composite obtained, by a laser technology (UV or IR), thermal stabilizers chosen from sterically hindered phenols or sterically amine type antioxidants congested (HALS) and shock modifiers. The function of these stabilizers is to prevent the thermal oxidation, the photoxidation and the consequent degradation of the matrix polyamide of the obtained composite.
    A secondary phosphite antioxidant can also be used.
    The thermal stabilizers and the secondary antioxidant are as defined for the polymer Pi.
    However, one and / or the other of the layers (polymer Pi and / or P2) of the structure of the invention may also comprise other compounds besides those which have just been mentioned. The composition of the invention (polymers P1 and / or P2) can in particular comprise at least one additional additive and / or at least one additional polymer.
    The additional additives may in particular be selected from adjuvants assisting the processing (or "processing aids").
    Among the adjuvants assisting the transformation include stearates, such as calcium or zinc stearates, natural waxes, polymers comprising tetrafluoroethylene (TFE).
    The proportion by weight of "Processing aids" is conventionally from 0.01 to 0.3% by weight, advantageously from 0.02 to 0.1% by weight, relative to the total weight of the composition. One and / or the other of the layers of the structure of the invention may further comprise one or more additional polymers, such a polymer being distinct from the polymer mentioned above. Alternatively, one and / or the other of the layers of the structure of the invention of the invention may be devoid of such additional polymer.
    The additional polymer may especially be chosen from a polyamide other than that defined above, a polyamide-block-ether, a polyetheramide, a polyesteramide, a phenylene polysulfide (PPS), a polyphenylene oxide (PPO), and mixtures thereof.
    The composition may thus contain up to 20% by weight, relative to the total weight of the composition, of at least one additional polymer.
    Tubular structure
    The tubular structure that is the subject of the invention may in particular be a tube or a pipe, or a connecting piece or connection between tubes, or between a tube and a device (such as a compressor, a condenser, a heat exchanger for example).
    The tubular structure may be formed of a single layer constituted by the composition described above. The total thickness of the structure of all the layers may for example range from 0.5 mm to 5 mm, preferably from 1 mm to 3 mm. The use of tubular structures according to the invention simplifies the design of circuits, allowing easy connection by welding (for example rotational welding, ultrasonic welding, laser welding or induction welding).
    Application to a vapor compression circuit
    A vapor compression circuit includes at least one evaporator, a compressor, a condenser and an expander, and heat transfer fluid transport lines between these elements. The evaporator and the condenser comprise a heat exchanger for heat exchange between a heat transfer fluid circulating in the circuit and another fluid or body. The facility may include a turbine to generate electricity (Rankine cycle).
    The vapor compression circuit may be integrated in an installation which may also optionally include at least one coolant circuit used to transmit heat (with or without a change of state) between the heat transfer fluid circuit and the fluid. or body to be heated or cooled. The installation may also optionally include two or more vapor compression circuits containing identical or different heat transfer fluids. For example, the vapor compression circuits may be coupled together.
    The vapor compression circuit operates in a conventional vapor compression cycle. The cycle comprises changing the state of the heat transfer fluid from a liquid phase (or two-phase liquid / vapor) to a vapor phase at a relatively low pressure, and then compressing the fluid in the vapor phase to a relatively high pressure. high, the change of state (condensation) of the heat transfer fluid from the vapor phase to the liquid phase at a relatively high pressure, and the reduction of the pressure to restart the cycle.
    In the case of a cooling process, heat from the fluid or the body that is cooled (directly or indirectly, via a coolant) is absorbed by the heat transfer fluid, during the evaporation of the latter, and this at a relatively low temperature compared to the environment. Cooling processes include air conditioning processes (with mobile installations, for example in vehicles, or stationary), refrigeration (with mobile installations for example in containers, or stationary) and freezing or cryogenics.
    In the case of a heating process, heat is transferred (directly or indirectly via a heat transfer fluid) from the heat transfer fluid, during the condensation thereof, to the fluid or to the body that is heating, and this at a relatively high temperature compared to the environment. The installation for implementing the heat transfer is called in this case "heat pump".
    A thermoplastic structure according to the invention can be used as a "vapor compression circuit element", i.e. as part of such a circuit having. Such a part comprises a light adapted to contain or transport the heat transfer fluid. The vapor compression circuit element in question is preferably a pipe or tubing (or a hose). Alternatively, it may be a connection or connector between tubings, or between tubing and compressor, or condenser, or heat exchanger or a part of a buffer capacity or a heat exchanger. The vapor compression circuit element may also be a heat exchanger as such (in which case it comprises at least two lumens for the circulation of two identical or different fluids, one to yield heat to the other).
    The heat transfer fluid may be contained or transported in gaseous, liquid or two-phase form in the above circuit element.
    Manufacture of thermoplastic materials of the structure of the invention
    The different layers of the structure of the invention may be prepared by any method which makes it possible to obtain a homogeneous mixture such as melt extrusion.
    More particularly, they may be prepared by melt blending of the polyamide (s), optionally plasticizer (s) and optionally products making it possible to obtain the crosslinked polyolefin (s). (s).
    Any additional additives and / or polymers may, in turn, be introduced, at the same time as the crystalline polyamide (s), plasticizer (s) and products making it possible to obtain the polyolefin (s). cross-linked (s) either at a later stage.
    Advantageously, the composition can be obtained in the form of granules by compounding, in particular by means of a twin-screw extruder, a co-kneader or an internal mixer.
    Heat transfer fluid
    By "heat transfer compound" or "heat transfer fluid" (or refrigerant, or refrigerant), is meant a compound, respectively a fluid, capable of absorbing heat by evaporating at low temperature and low pressure and provide heat by condensing at high temperature and high pressure, in a vapor compression circuit. In general, a heat transfer fluid may comprise one, two, three or more than three heat transfer compounds.
    In addition, the heat transfer fluid may optionally include one or more additives that are not heat transfer compounds for the intended application.
    The heat transfer compounds may be hydrocarbon compounds, ethers, hydrofluoroethers, hydrofluorocarbons or fluoroolefins or HFOs. Hydrofluorocarbons and fluoroolefins are preferred, and more particularly fluoroolefins. Fluoropropenes, fluoropropanes and fluoroethans are preferred.
    Examples of preferred heat transfer compounds, used individually or in admixture, are 1,3,3,3-tetrafluoropropene (R-1234ze), 2,3,3,3-tetrafluoropropene (R-1234yf), 1,2 3,3,3-pentafluoropropene (R-1225ye), 1,1,3,3-tetrafluoropropene (R-1234zc), 3,3,3-trifluoropropene (R-1243zf), 2,3,3-trifluoropropene (R- 1243yf), 1,1,1,2-tetrafluoroethane (R-134a), 1,1,2,2-tetrafluoroethane (R-134), pentafluoroethane (R-125), difluoromethane (R-32) , 1,1-difluoroethane (R-152a), 1,1,1,2,3,3,3-heptafluoropropane (R-227ea), 1,1,1-trifluoropropane (R-263), 1,1,1,3,3,3-hexafluoropropane (R-236fa), 1,1,1,3,3-pentafluoropropane (R-245fa), 1,1,1,3,3-pentafluorobutane ( R-365mfc) and trifluoroiodomethane.
    The above compounds can also be used in admixture with ammonia or carbon dioxide.
    According to a preferred embodiment, the heat transfer fluid is R-134a, or R-1234yf or R-1234ze, the latter being particularly preferred.
    Mixtures of R-1234yf or R-1234ze and ammonia, and R-1234yf or R-1234ze and carbon dioxide, are also preferred, especially for stationary air conditioning.
    The additives may especially be chosen from lubricants, nanoparticles, stabilizers, surfactants, tracer agents, fluorescent agents, odorants and solubilizing agents.
    The stabilizer (s), when present, preferably represent at most 5% by weight in the heat transfer composition. Among the stabilizers, there may be mentioned in particular nitromethane, ascorbic acid, terephthalic acid, azoles such as tolutriazole or benzotriazole, phenol compounds such as tocopherol, hydroquinone, t-butyl hydroquinone, 2,6-di-tert-butyl-4-methylphenol, epoxides (optionally fluorinated or perfluorinated alkyl or alkenyl or aromatic) such as n-butyl glycidyl ether, hexanediol diglycidyl ether, allyl glycidyl ether, butylphenylglycidyl ether, phosphites, phosphonates, thiols and lactones. Lubricants that may be used include oils of mineral origin, silicone oils, paraffins of natural origin, naphthenes, synthetic paraffins, alkylbenzenes, poly-alpha olefins, polyalkylene glycols (PAG), polyol esters and / or polyvinyl ethers.
    According to the invention, it is particularly preferred that the heat transfer fluid circulating in the vapor compression circuit comprises a PAG lubricant or a POE lubricant.
    According to a particularly preferred embodiment of the invention, the heat transfer fluid is R-1234yf or R-1234ze supplemented with PAG lubricant (and optionally additional additives).
    Among the lubricants PAG, it is possible to use those described in US 2010/0282999, which is expressly referred to herein. These lubricants correspond to the formula Rr (OR3) n-R2, in which R1 and R2 are identical or different and represent a hydrogen atom, a C1-C5 alkyl group or a C2-C5 acyl group, R3 represents a C2-C4 alkylene group, and the molar proportion of C2 alkylene groups in the R3 units is at most 30%. The hydroxyl value is preferably at most 100 mgKOH / g, or 50, 30 or 10 mgKOH / g. The number-average molecular weight of the PAG is preferably 500 to 3000, or 600 to 2000 or 600 to 1500.
    Among the PAG lubricants, it is also possible to use those described in US 2010/0175421, which is expressly referred to herein. These lubricants correspond to the formula R 1 - [(OR 2) m -R 3] n, in which R 1 represents a hydrogen atom, a hydrocarbon group having 1 to 10 carbon atoms, an acyl group having 2 to 10 carbon atoms, a hydrocarbon group having 2 to 6 binding sites and 1 to 10 carbon atoms or an oxygen-containing hydrocarbon group having 1 to 10 carbon atoms, R 2 is an alkylene group having 2 to 4 carbon atoms, R 3 is a hydrogen atom, a hydrocarbon group having 1 to 10 carbon atoms, an acyl group having 2 to 10 carbon atoms, or a hydrocarbon group containing an oxygen atom having 1 to 10 carbon atoms, n represents an integer from 1 to 6 and m is a number such that the average value mxn is from 6 to 80. Examples of such PAGs are polypropylene glycol dimethyl ether, polyethylene-polypropylene glycol dimethyl ether copolymer, polyethylene-polypropylene glycol copolymer m thylbutyléther and polypropylene glycol diacetate. The hydroxyl value is preferably 5 mgKOH / g or less, or 3 mgKOH / g or less, or 1 mgKOH / g or less. The number-average molecular weight of the PAG is preferably 500 to 3000, or 600 to 2500.
    Among the PAG lubricants, it is also possible to use those described in WO 2010/075046, which is expressly referred to herein. These lubricants correspond to the formula RX (RaO) x (RbO) y Rc, in which R is chosen from alkyl groups having from 1 to 10 carbon atoms, aliphatic hydrocarbon groups having from 2 to 6 valences, and substituents comprising a heterocycle in which the one or more heteroatoms are oxygen, X is selected from O and S, Ra is a C2 alkylene group, Rb is a C3 alkylene group, Rc is the same as R or is H, x and y are 0 or an integer less than or equal to 100, independently. The sum x + y is an integer of 5 to 100. The aliphatic hydrocarbon groups include, in particular, alkanes, alkenes, alkynes, and in particular methyl, butyl and propyl groups. The lubricant can be a homopolymer of oxypropylene, linear. Alkoxy and especially methoxy termini are preferred. The kinematic viscosity is preferably at least 30 cSt, or 20 cSt, or 10 cSt at 40 ° C, or a viscosity number of at least 150, or 120 or 100. The total acid value is preferably less than 0.03, or 0.02, or 0.01 mgKOH / g. As nanoparticles, it is possible in particular to use carbon nanoparticles, metal oxides (copper, aluminum), T1O2, Al2O3, M0S2, etc. As tracer agents (which can be detected), mention may be made of deuterated hydrofluorocarbons or no, deuterated hydrocarbons, perfluorocarbons, fluoroethers, brominated compounds, iodinated compounds, alcohols, aldehydes, ketones, nitrous oxide and combinations thereof. The tracer agent is different from the one or more heat transfer compounds composing the heat transfer fluid. As solubilizing agents, mention may be made of hydrocarbons, dimethyl ether, polyoxyalkylene ethers, amides, ketones, nitriles, chlorocarbons, esters, lactones, aryl ethers, fluoroethers and the like. , 1-trifluoroalcanes. The solubilizing agent is different from the one or more heat transfer compounds composing the heat transfer fluid. As fluorescent agents, mention may be made of naphthalimides, perylenes, coumarins, anthracenes, phenanthracenes, xanthenes, thioxanthenes, naphthoxanhthenes, fluoresceins and derivatives and combinations thereof. As odorants, mention may be made of alkyl acrylates, allyl acrylates, acrylic acids, acrylresters, alkyl ethers, alkyl esters, alkynes, aldehydes, thiols, thioethers, disulfides, allyl isothiocyanates and alkanoic acids. amines, norbornenes, norbornene derivatives, cyclohexene, heterocyclic aromatic compounds, ascaridole, o-methoxy (methyl) phenol and combinations thereof.
    With respect to automotive air conditioning, it is preferred to use a single heat transfer compound (rather than a mixture) and a single lubricant (rather than a mixture), for stability issues in the air conditioning circuit. vapor compression.
    EXAMPLE
    Example 1 - Permeability properties to fluorinated refrigerants
    In this example, the permeability to fluorinated refrigerants (R-1234yf) of a tubular structure (according to the invention) consisting of a composition comprising a copolyamide of formula 11 / 10T in an inner layer (polymer P1) and of a composition comprising a polyamide of formula PA610 with fibers (60% by mass of glass fibers) in an outer layer (polymer P2) with a standard tubular structure of Veneer type comprising either 200 or 300 microns of impact modified PA 6, corresponding to the product marketed by DuPont under the name Zytel® ST 811.
    The flux measurements were made on films of the same composition as the layers of the tubular structures with a permeation cell, by a Lyssy GPM500 / GC coupling at a temperature of 23 ° C. and 0% relative humidity. The upper face of the cell is swept by the test gas, and the flux diffusing through the film in the lower part is measured by gas chromatography. Helium is used as the carrier gas sweeping the lower part.
    The permeation of the tubular structures is calculated by the usual permeation law of a multilayer, namely
    e and P are the thickness and the permeability of the multilayer structure ei and Pi are the thicknesses and the permeabilities of each of the layers of the structure
    The results of the calculations are reproduced in Tables 1 below. The refrigerant flows are expressed in cm3 / m2 / 24 h / atm.
    Table 1 - Results for the R-1234vf
    The structure of the invention is better barrier to R-1234yf than the Veneer structure.
    权利要求:
    Claims (26)
    [1" id="c-fr-0001]
    A tubular structure for transporting heat transfer fluid, in particular refrigerant, comprising at least: i) a layer (1) in contact with the fluid comprising at least one semi-crystalline thermoplastic polymer Pi of greater than or equal to 160 ° C in particular greater than or equal to 170 ° C as determined according to standard 11357-3 (2013) or amorphous Tgi greater than or equal to 100 ° C, preferably 120 ° C in particular 140 ° C as determined according to the standard 11357-2 (2013), said layer (1) being free of fibers, ii) a layer (2) comprising at least: (a) a semi-crystalline thermoplastic polymer P2, in particular an upper Tf2 polyamide or equal to 170 ° C or amorphous of Tg2 greater than or equal to 100 ° C, or a polyolefin of Tf greater than 100 ° C; (b) continuous fibers, the polymer P2 being identical to Pi or different from Pi in which case the polymers Pi and P2 adhere at least partially to each other.
    [2" id="c-fr-0002]
    2. Structure according to claim 1, characterized in that said polymer Pi is chosen from polyamides and EVOH, in particular polyamides.
    [3" id="c-fr-0003]
    3. Structure according to one of claims 1 or 2, characterized in that said polymer Pi is a semi-crystalline polyamide.
    [4" id="c-fr-0004]
    4. Structure according to one of claims 1 to 3, characterized in that said polymer P2 is selected from polyamides and polyolefins.
    [5" id="c-fr-0005]
    5. Structure according to one of claims 1 to 4, characterized in that said polymer P2 is a semi-crystalline polyamide.
    [6" id="c-fr-0006]
    6. Structure according to one of claims 1 to 5, characterized in that said polymers Pi and P2 are semi-crystalline polyamides.
    [7" id="c-fr-0007]
    7. Structure according to one of claims 1 to 6, characterized in that said polymer P2 is an amorphous polyamide.
    [8" id="c-fr-0008]
    8. Structure according to claim 1, characterized in that said polymer Pi is a polyamide chosen from polyphthalamides, semi-aromatic polyamides, in particular A / T, A / 10T, A / 6T, XY / 10T and XY / 6T. , PA6, PA66, PA6 / 66, PA610, PA612, a C4-C8 short chain polyamide, in particular derived from the polymerization of lactams or C4-C8 aminocarboxylic acids, or the polymerization of at least one diamine and at least one less a dicarboxylic acid whose average number of carbon atoms is from C4 to C8, and a PA / polyolefin mixture, said polyolefin may be functionalized (all or part) or not, in particular an Orgalloy®.
    [9" id="c-fr-0009]
    9. Structure according to claim 8, characterized in that said polymer Pt is a polyamide chosen from polyphthalamides, semi-aromatic polyamides,. . in particular T1 / 10T, 612 / 10T, 11 / 6T, PA6, PA66, PA6 / 66, PA610, PA612, a C4-C8 short chain polyamide, and a PA / polyolefin mixture, said polyolefin may be functionalized or not.
    [10" id="c-fr-0010]
    10. Structure according to one of claims 8 or 9, characterized in that said polymer Pi is a polyamide selected from semi-aromatic polyamides, including 11 / 1T, 612 / 10T, 11 / 6T, PA6, PA66, PA6 / 66, PA610, PA612, a C4-C8 short chain polyamide, and a PA / polyolefin mixture, wherein said polyolefin can be functionalized or not.
    [11" id="c-fr-0011]
    11. Structure according to one of claims 8 to 10, characterized in that said polymer Pi is a polyamide chosen from polyphthalamides, polyamides semi-aromatic, especially i 171OT, 612 / 10T, 11 / 6T, PA6, PA66, RA6 / 66, a C4-C8 short chain polyamide, and a PA / polyolefin mixture, said polyolefin may be functionalized or not, excluding PA610 and PA612.
    [12" id="c-fr-0012]
    12. Structure according to one of claims 8 to 11, characterized in that said polymer Pi is a polyamide selected from semi-aromatic polyamides, including 11/1 OT, 612 / 10T, 11 / 6T, PA6, PA66, PA6 / 66, a C4-C8 short chain polyamide, and a PA / polyolefin mixture, wherein said polyolefin may be functionalized or not, excluding PA610 and PA612.
    [13" id="c-fr-0013]
    13. Structure according to one of claims 1 to 12, characterized in that said polymer P2 is a polyamide chosen from polyphthalamides, semi-aromatic polyamides, in particular 11 / 1OT and 11 / 6T, PA11, PA12, PA6, PA66. , PA6 / 66, PA610, PA612.
    [14" id="c-fr-0014]
    14. Structure according to one of claims 1 to 13, characterized in that said polymer Pi and / or said polymer P2, comprises at least one binder.
    [15" id="c-fr-0015]
    15. Structure according to one of claims 1 to 14, characterized in that it comprises at least a third outer layer (3), said layer being in contact with the layer (2) and comprising an elastomer and / or a polymer P3 identical or different from Pi and adhering at least partially to P2.
    [16" id="c-fr-0016]
    16. Structure according to one of claims 1 to 15, characterized in that the continuous fibers are chosen from: - mineral fibers - carbon fibers and carbon nanotubes - polymer or polymer fibers, - or mixtures aforementioned fibers.
    [17" id="c-fr-0017]
    17. Structure according to one of claims 1 to 16, wherein: the mineral fibers are selected from: silica fibers such as glass fibers, especially of type E, R or S2; boron fibers; ceramic fibers, especially silicon carbide, boron carbide, boron carbonitride, silicon nitride, boron nitride; basalt fibers; fibers or filaments based on metals and their alloys; fibers based on metal oxides; metallized carbon fibers and metallized glass fibers or mixtures of the fibers mentioned, and the polymeric fibers are chosen from: thermosetting polymer fibers thermoplastic polymer fibers polyamide fibers corresponding to one of the following polyamides: 6, 66 , 610, 612, 46, 410, 1010, 1012, 11 and 12 aramid fibers and aromatic polyamides such as those corresponding to one of the formulas: PPD.T, MPD.I, PAA and PPA or mixtures thereof fibers mentioned above.
    [18" id="c-fr-0018]
    18. Structure according to one of claims 1 to 17, wherein the proportion by weight of fibers in the layer comprising P2 is from 30 to 80%, preferably from 50 to 70%.
    [19" id="c-fr-0019]
    19. Structure according to one of claims 1 to 18, wherein the refrigerant is selected from hydrocarbons, hydrofluorocarbons, ethers, hydrofluoroethers or fluoroolefins, including fluoropropenes, fluoropropanes and fluoroethanes; preferably from 1,3,3,3-tetrafluoropropene, 2,3,3,3-tetrafluoropropene, 1,2,3,3,3-pentafluoropropene, 1,1,3,3-tetrafluoropropene, 3,3,3-trifluoropropene, 2,3,3-trifluoropropene, 1,1,1,2-tetrafluoroethane, 1,1,2,2-tetrafluoroethane, pentafluoroethane, difluoromethane, 1,1,1,2-tetrafluoroethane, 1,1,2,2-tetrafluoroethane, difluoroethane, 1,1,1,2,3,3,3-heptafluoropropane, 1,1,1-trifluoropropane, 1,1,1,3,3,3-hexafluoropropane, 1,1,1, 3,3-pentafluoropropane, 1,1,1,3,3-pentafluorobutane, trifluoroiodomethane and mixtures thereof; and particularly preferably said refrigerant being 2,3,3,3-tetrafluoropropene (1234yf) or 1,3,3,3-tetrafluoropropene (1234ze).
    [20" id="c-fr-0020]
    20. Structure according to one of claims 1 to 19, wherein the refrigerant is added with a lubricant, preferably selected from mineral oils, silicone oils, paraffins of natural origin, naphthenes, paraffins synthetic, alkylbenzenes, poly-alpha olefins, polyalkylene glycols, polyol esters and / or polyvinyl ethers; the lubricant is more preferably a polyalkylene glycol or a polyol ester.
    [21" id="c-fr-0021]
    21. The structure of claim 20, wherein said lubricant is in a proportion by weight of 0.5% to 50%, especially 1 to 15%.
    [22" id="c-fr-0022]
    22. Structure according to one of claims 1 to 21, which is a vapor compression circuit element for containing or transporting a refrigerant, said vapor compression circuit element preferably being a connecting member or a pipe.
    [23" id="c-fr-0023]
    23. Structure according to one of claims 1 to 22, wherein the vapor compression circuit is integrated in a device selected from mobile or stationary air conditioning devices, refrigeration devices, freezing devices, heating devices. heat pump and Rankine cycles; and preferably is integrated in a car air conditioning device.
    [24" id="c-fr-0024]
    24. A method of manufacturing the structure according to one of claims 1 to 23, characterized in that it comprises at least one extrusion step of the layer (1).
    [25" id="c-fr-0025]
    25. Manufacturing process according to claim 24, characterized in that it comprises the following successive steps: a. manufacturing said layer (1) by extrusion through an annular die and b. depositing on said layer (1) of said outer layer (2) in the molten state by the rolling technique laminated with polymer impregnated fibers P2 in the molten state with one or more angles of orientation relative to the axis of said structure and c. cooling said structure.
    [0026]
    Use of a thermoplastic structure according to one of claims 1 to 23 for the transport of a refrigerant in a vapor compression circuit.
    类似技术:
    公开号 | 公开日 | 专利标题
    JP2018168374A|2018-11-01|Use of semi-aromatic copolyamide for transporting refrigerant fluid
    EP3390039B1|2019-06-12|Multilayer structure comprising continuous fibers for transporting heat transfer fluid
    EP2956301B1|2021-03-24|Thermoplastic structure for transporting refrigerant fluid
    US20220082186A1|2022-03-17|Use of semi-aromatic copolyamide for transporting refrigerant fluid
    EP3663081B1|2021-05-26|Multilayer tubular structure intended for transporting an air-conditioning fluid
    EP3466681B1|2019-08-07|Multilayer material with resistance to ageing and hot burst, for high temperature automotive applications
    同族专利:
    公开号 | 公开日
    CN108430760A|2018-08-21|
    US20180361699A1|2018-12-20|
    KR20180093996A|2018-08-22|
    EP3390039B1|2019-06-12|
    JP2019501797A|2019-01-24|
    JP6983782B2|2021-12-17|
    CN108430760B|2020-11-03|
    EP3390039A1|2018-10-24|
    US20200101689A1|2020-04-02|
    WO2017103466A1|2017-06-22|
    FR3044959B1|2017-12-08|
    US10471677B2|2019-11-12|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE102008037490A1|2008-10-29|2010-05-06|Contitech Fluid Automotive Gmbh|Cool water tube for vehicle construction, comprises an internal layer made of a first polymer material that is completely free from fibers, and an external layer made of second polymer materials that are mixed with glass fibers|
    EP2578391A1|2010-06-02|2013-04-10|The Yokohama Rubber Company, Limited|Refrigerant-transporting hose|
    PL1717022T3|2005-04-29|2014-07-31|Arkema France|Polyamide-based multilayer tube for transferring fluids|
    US8003202B2|2006-06-16|2011-08-23|E.I. Du Pont De Nemours And Company|Semiaromatic polyamide composite article and processes for its preparation|
    ITTO20080404A1|2008-05-27|2009-11-28|Dayco Fluid Technologies Spa|CABLE ELEMENT FOR THE TRANSPORT OF A REFRIGERANT FLUID IN A MOTOR VEHICLE|
    US8211517B2|2009-06-08|2012-07-03|Ei Du Pont De Nemours And Company|Multi-layered coextruded tube|
    FR3002233B1|2013-02-18|2016-01-22|Arkema France|THERMOPLASTIC STRUCTURE FOR TRANSPORTING REFRIGERANT FLUID|
    FR3002180B1|2013-02-18|2017-12-29|Arkema France|USE OF SEMI-AROMATIC COPOLYAMIDE FOR THE TRANSPORT OF REFRIGERANT FLUID|JP6983563B2|2017-07-24|2021-12-17|株式会社ブリヂストン|Refrigerant transport hose|
    FR3089147B1|2018-12-04|2020-11-06|Arkema France|MULTI-LAYER TUBULAR STRUCTURE INTENDED FOR THE TRANSPORT OF AIR CONDITIONING FLUID|
    CN110878194B|2019-10-16|2020-11-17|珠海格力电器股份有限公司|R13I 1-containing environment-friendly mixed refrigerant and heat exchange system|
    CN110878195B|2019-10-16|2020-11-27|珠海格力电器股份有限公司|Coolant containing trifluoroiodomethane, mixture containing coolant and heat exchange system|
    法律状态:
    2016-11-11| PLFP| Fee payment|Year of fee payment: 2 |
    2017-06-16| PLSC| Publication of the preliminary search report|Effective date: 20170616 |
    2017-11-13| PLFP| Fee payment|Year of fee payment: 3 |
    2019-11-14| PLFP| Fee payment|Year of fee payment: 5 |
    2021-09-10| ST| Notification of lapse|Effective date: 20210806 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1562378A|FR3044959B1|2015-12-15|2015-12-15|MULTILAYER STRUCTURE COMPRISING CONTINUOUS FIBERS FOR TRANSPORTING HEAT TRANSFER FLUID|FR1562378A| FR3044959B1|2015-12-15|2015-12-15|MULTILAYER STRUCTURE COMPRISING CONTINUOUS FIBERS FOR TRANSPORTING HEAT TRANSFER FLUID|
    CN201680074762.3A| CN108430760B|2015-12-15|2016-12-14|Multilayer structure comprising continuous fibers for transporting a heat transfer fluid|
    EP16825840.8A| EP3390039B1|2015-12-15|2016-12-14|Multilayer structure comprising continuous fibers for transporting heat transfer fluid|
    PCT/FR2016/053412| WO2017103466A1|2015-12-15|2016-12-14|Multilayer structure comprising continuous fibers for transporting heat transfer fluid|
    US15/780,089| US10471677B2|2015-12-15|2016-12-14|Multilayer structure comprising continuous fibers for transporting heat transfer fluid|
    KR1020187019470A| KR20180093996A|2015-12-15|2016-12-14|A multi-layer tubular structure comprising continuous fibers for conveying a heat transfer fluid|
    JP2018531206A| JP6983782B2|2015-12-15|2016-12-14|Multilayer structure containing continuous fibers for heat transfer fluid|
    US16/592,890| US20200101689A1|2015-12-15|2019-10-04|Multilayer structure for transporting heat transfer fluid|
    [返回顶部]