JP2011224988A - Laminated tube - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a laminated tube excellent in inter-layer adhesion and impermeability to chemical liquids, especially to a concentrated alcohol containing gasoline.SOLUTION: The laminated tube includes at least the following three layers: a layer composed of an aliphatic polyamide (A) that has a number ratio of 5 or more in methylene/amide group and a saturation factor of 1.4% or higher in water absorption under water of 23°C; a layer composed of a polyamide (B) containing a diamine unit having 50 mol% or more per total diamine of a 9-13C aliphatic diamine unit and an oxamide unit comprising a dicarboxylic acid unit containing 60 mol% or more of oxalic acid unit per total dicarboxylic acid unit; and a layer (c) composed of a polyamide resin composition containing 0.5-5 pts.mass of a polycarbonate per 100 pts.mass of the polyamide (A) and polyamide (B) combined.

Description

  The present invention relates to a laminated tube excellent in interlayer adhesion, chemical solution permeation prevention, particularly permeation prevention for high-concentration alcohol-containing gasoline.

  In the past, automobile piping tubes were rusting due to antifreezing agents on roads, and in recent years, in response to requests for global warming prevention and energy saving, the main material is excellent in rust prevention. Substitution with lightweight resin is progressing. Resin used as a tube for piping usually includes polyamide-based resin, saturated polyester-based resin, polyolefin-based resin, thermoplastic polyurethane-based resin, etc., but in the case of a single-layer tube using these, heat resistance The applicable range is limited due to insufficient chemical resistance and the like.

  From the viewpoint of saving gasoline consumption and improving performance, automobile piping tubes include low-boiling alcohols such as methanol and ethanol, or oxygen-containing gasoline blended with ethers such as methyl-t-butyl ether (MTBE). Be transported. Furthermore, in recent years, strict exhaust gas regulations including prevention of leakage into the atmosphere due to diffusion of volatile hydrocarbons and the like through piping tube partition walls have been implemented from the viewpoint of preventing environmental pollution. In the future, since stricter regulations are imposed, it is desirable to suppress the fuel that permeates and evaporates from the piping tube partition wall to the limit. For such strict regulations, conventionally used single-layer tubes using polyamide-based resins, particularly polyamide 11 or polyamide 12 excellent in strength, toughness, chemical resistance and flexibility, The permeation-preventing property with respect to chemicals is not sufficient, and further improvements are required.

  As a method for solving this problem, resins having good chemical permeation preventive properties such as saponified ethylene / vinyl acetate copolymer (EVOH), polymetaxylylene adipamide (polyamide MXD6), polybutylene terephthalate (PBT), poly Butylene naphthalate (PBN), polyphenylene sulfide (PPS), polyvinylidene fluoride (PVDF), ethylene / tetrafluoroethylene copolymer (ETFE), ethylene / chlorotrifluoroethylene copolymer (ECTFE), tetrafluoroethylene / hexa Fluoropropylene copolymer (TFE / HFP, FEP), tetrafluoroethylene / hexafluoropropylene / vinylidene fluoride copolymer (TFE / HFP / VDF, THV), tetrafluoroethylene / perfluoro (alkylbiphenyl) Laminated tubes ether) copolymer (PFA) are arranged has been proposed (e.g., see Patent Document 1.).

Furthermore, in recent years, studies on the use of alcohol-containing gasoline (biofuel) in which alcohol such as ethanol derived from biomass (bioethanol) is added to gasoline are being promoted from the viewpoint of exhaustion of gasoline resources and environmental conservation. For example, as biofuels, currently gasoline containing bioethanol, bioethanol 10% mixed gasoline (E10), bioethanol 85% mixed gasoline (E85), bioethanol 100% (E100) are Brazil, North America, China, etc. Therefore, there is an urgent need to develop a flex fuel vehicle piping system that can be used for both bioethanol-mixed gasoline and gasoline.
However, polyamide 6, polyamide 66, polymetaxylylene adipamide (polyamide MXD6) and other polyamides and saponified ethylene / vinyl acetate copolymer (EVOH) satisfy ethanol vapor permeation resistance, but ethanol Because gasoline with iso-high concentration alcohol has insufficient permeation resistance to alcohol, it is difficult to fully meet exhaust gas regulations that will be strengthened in the future, and materials with higher barrier performance are desired. .

For polyesters such as polybutylene terephthalate (PBT) and polybutylene naphthalate (PBN), it is necessary to improve the hydrolysis resistance of the material and to laminate it with a flexible material. Polyphenylene sulfide (PPS) is an alcohol-containing material. Although it has excellent permeation resistance to gasoline, it is difficult to join and adhere to other members, and it is not suitable for a laminated structure.
For fluororesins, the permeation resistance to hydrocarbons is not so good, but the permeation resistance to alcohol is excellent, and it is one of the material members that have excellent barrier performance against high-concentration alcohol-containing gasoline. It can be considered as one. In recent years, the development of fluororesins that have adhesive properties with polyamide has become active, but the use of halogen-containing compounds has been progressing in terms of environmental friendliness, and high specific gravity and high cost. There is a problem, and there is a need for a laminated tube that is excellent in permeation resistance to gasoline containing high-concentration alcohol, is halogen-free, and is low in cost.

  On the other hand, Patent Document 2 discloses a molding material for fuel parts made of polyamide containing an oxamide bond unit. The document describes that polyamides containing oxamide bond units have excellent fuel barrier properties, low water absorption, and are suitable as materials for fuel parts, and data on the permeability coefficient of gasoline containing high-concentration alcohol is disclosed. Has been. In Patent Document 3, the dicarboxylic acid component is composed of oxalic acid, the diamine component is composed of 1,9-nonanediamine and 2-methyl-1,8-octanediamine, and 1,9-nonanediamine and 2-methyl-1, A fuel tube comprising a polyamide resin layer having a molar ratio of 8-octanediamine of 1:99 to 99: 1, and further, the polyamide resin layer and a fluorine resin, a high-density polyethylene resin, and a polyamide 11 and / or a fuel tube comprising a layer selected from a resin comprising a plasticizer in polyamide 12 is disclosed. There is no disclosure or technical suggestion regarding data on interlayer adhesion in laminated tubes.

US Pat. No. 5,554,425 International Patent Publication No. 2008-123534 JP 2009-299721 A

  An object of the present invention is to solve the above-mentioned problems and to provide a laminated tube excellent in interlayer adhesion and chemical solution permeation prevention properties, in particular, permeation prevention properties for high-concentration alcohol-containing gasoline.

In order to solve the above problems, the present inventors have conducted intensive studies,
A laminated tube consisting of at least three layers, including a (a) layer made of polyamide (A), a (b) layer made of polyamide (B), and a (c) layer made of polyamide (C),
The polyamide (A) is an aliphatic polyamide having a methylene group number / amide group number ratio of 5 or more and a methylene group number / amide group number of 5 or more and a saturated water absorption at 23 ° C. in water of 1.4% or more,
The polyamide (B) is a diamine unit containing 50 mol% or more of an aliphatic diamine unit having 9 to 13 carbon atoms based on all diamine units, and a dicarboxylic acid containing 60 mol% or more oxalic acid units based on all dicarboxylic acid units. A polyamide containing an oxamide bond unit comprising an acid unit;
The laminated tube, which is a polyamide resin composition containing 0.5 to 5 parts by mass of polycarbonate with respect to a total of 100 parts by mass of polyamide (C) and polyamide (B), has interlayer adhesion and chemical penetration. It has been found that it has excellent properties such as low temperature impact resistance, heat resistance, chemical resistance, etc.

That is, the present invention
A laminated tube consisting of at least three layers, including a (a) layer made of polyamide (A), a (b) layer made of polyamide (B), and a (c) layer made of polyamide (C),
The polyamide (A) is an aliphatic polyamide having a methylene group number / amide group number ratio of 5 or more and a methylene group number / amide group number of 5 or more and a saturated water absorption at 23 ° C. in water of 1.4% or more,
The polyamide (B) is a diamine unit containing 50 mol% or more of an aliphatic diamine unit having 9 to 13 carbon atoms based on all diamine units, and a dicarboxylic acid containing 60 mol% or more oxalic acid units based on all dicarboxylic acid units. A polyamide containing an oxamide bond unit comprising an acid unit;
The polyamide (C) relates to a laminated tube which is a polyamide resin composition containing 0.5 to 5 parts by mass of polycarbonate with respect to 100 parts by mass in total of polyamide (A) and polyamide (B).

  The laminated tube of the present invention has good interlaminar adhesion, and further has excellent chemical solution permeation prevention properties, particularly permeation prevention properties for high-concentration alcohol-containing gasoline. Therefore, the laminated tube of the present invention can be used for various fuels, and its utility value is extremely large.

The present invention is described in detail below.
[Polyamide (A)]
The polyamide (A) used in the present invention is an aliphatic polyamide having a ratio of the number of methylene groups to the number of amide groups of 5 or more and a saturated water absorption of 23% in water at 1.4% or more in the main chain. It has an amide bond (—CONH—), and the ratio of the number of methylene groups ([CH ₂ ]) to the number of amide groups ([NHCO]) ([CH ₂ ] / [NHCO]) (hereinafter, the ratio of the number of methylene groups to the number of amide groups) [CH ₂ ] / [NHCO] may be referred to as 5) or higher, the temperature is 23 ° C., the saturated water absorption in water is 1.4% or higher, and lactam, aminocarboxylic acid, or aliphatic diamine It can be obtained by polymerizing or copolymerizing a nylon salt composed of an aliphatic dicarboxylic acid with a known method such as melt polymerization, solution polymerization or solid phase polymerization.
Specifically, the saturated water absorption is obtained by molding a test piece having a length of 80 mm, a width of 80 mm, and a thickness of 1 mm, and measuring the pre-test mass (mass before water absorption) of the test piece in an absolutely dry state after molding. The test piece is immersed in water at 23 ° C. for 1,000 hours. Thereafter, the test piece is taken out of the water, the surface adhering moisture is wiped off, and left in a constant temperature and humidity (23 ° C., 50 RH%) atmosphere for 30 minutes, and then the post-test mass (mass after water absorption) of the test piece is measured. The increment of the mass after water absorption with respect to the mass before water absorption of the test piece is defined as the water absorption amount, and the ratio of the water absorption amount with respect to the mass before water absorption is defined as the saturated water absorption rate (%).

  Examples of lactams include caprolactam, enantolactam, undecane lactam, dodecane lactam, α-pyrrolidone, α-piperidone, and aminocarboxylic acids include 6-aminocaproic acid, 7-aminoheptanoic acid, 9-aminononanoic acid, and 11-aminoundecane. Examples include acid and 12-aminododecanoic acid. These can use 1 type (s) or 2 or more types.

  Examples of the aliphatic diamine constituting the nylon salt include 1,2-ethanediamine, 1,3-propanediamine, 1,4-butanediamine, 1,5-pentanediamine, 1,6-hexanediamine, 1,7- Heptanediamine, 1,8-octanediamine, 1,9-nonanediamine, 1,10-decanediamine, 1,11-undecanediamine, 1,12-dodecanediamine, 1,13-tridecanediamine, 1,14-tetradecane Diamine, 1,15-pentadecanediamine, 1,16-hexadecanediamine, 1,17-heptadecanediamine, 1,18-octadecanediamine, 1,19-nonadecanediamine, 1,20-eicosanediamine, 2- / 3-methyl-1,5-pentanediamine, 2-methyl-1,8-octanediamine, 2, , 4 / 2,4,4-trimethyl-1,6-hexanediamine, 5-methyl-1,9-nonanediamine or the like. These can use 1 type (s) or 2 or more types.

  The aliphatic dicarboxylic acids constituting the nylon salt include adipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, undecanedioic acid, dodecanedioic acid, tridecanedioic acid, tetradecanedioic acid, pentadecanedioic acid, hexadecanedioic acid. , Octadecanedioic acid, eicosanedioic acid and the like. These can use 1 type (s) or 2 or more types.

  Polyamide (A) includes polycaproamide (polyamide 6), polyundecanamide (polyamide 11), polydodecanamide (polyamide 12), polyethylene adipamide (polyamide 26), polytetramethylene adipamide (polyamide 46). , Polyhexamethylene adipamide (polyamide 66), polyhexamethylene azelamide (polyamide 69), polyhexamethylene sebacamide (polyamide 610), polyhexamethylene undecamide (polyamide 611), polyhexamethylene dodecamide ( Polyamide 612), polynonamethylene adipamide (polyamide 96), polynonamethylene azelamide (polyamide 99), polynonamethylene sebamide (polyamide 910), polynonamethylene undecamide (polyamide 911), Linonamethylene dodecamide (polyamide 912), polydecamethylene adipamide (polyamide 106), polydecamethylene azelamide (polyamide 109), polydecamethylene sebamide (polyamide 1010), polydecamethylene dodecamide (polyamide 1012) ), Polydodecamethylene adipamide (polyamide 126), polydodecamethylene azelamide (polyamide 129), polydodecamethylene sebamide (polyamide 1210), and polydodecamethylene dodecamide (polyamide 1212) Examples thereof include copolymers using several kinds of raw material monomers for forming the.

Among these, polycaproamide (polyamide 6), polyundecanamide (polyamide 11), polydodecanamide (polyamide 12), polyhexamethylene adipamide (polyamide 66), polyhexamethylene azelamide (polyamide 69), poly Hexamethylene sebacamide (polyamide 610), polyhexamethylene undecamide (polyamide 611), polyhexamethylene dodecane (polyamide 612), polynonamethylene dodecamide (polyamide 912), polydecamethylene sebacamide (polyamide 1010) ), Polydecamethylene dodecamide (polyamide 1012), polydodecamethylene dodecamide (polyamide 1212), and copolymers using several raw material monomers to form these are preferred. Polycaproamide (polyamide) ), Polyhexamethylene adipamide (polyamide 66), polyhexamethylene sebamide (polyamide 610), polyhexamethylene dodecamide (polyamide 612), polydecamethylene sebacamide (polyamide 1010), polydecamethylene dodecamide (Polyamide 1012), polydodecane methylenedodecanamide (polyamide 1212), polyundecanamide (polyamide 11), and at least one selected from the group consisting of polydodecanamide (polyamide 12) are more preferable.
For example, in the case of polycaproamide (polyamide 6) and polyhexamethylene adipamide (polyamide 66), [CH ₂ ] / [NHCO] = 5, in the case of polyhexamethylene sebacamide (polyamide 610), [CH ₂ ] / [NHCO] = 7, polyhexamethylene dodecamide (polyamide 612), [CH ₂ ] / [NHCO] = 8, polydecamethylene sebacamide (polyamide 1010), [CH ₂ ] / [ In the case of NHCO] = 9, polydecamethylene dodecamide (polyamide 1012), [CH ₂ ] / [NHCO] = 10, in the case of polydecamethylene dodecamide (polyamide 1212), [CH ₂ ] / [NHCO] = 11 In the case of polyundecanamide (polyamide 11), [CH ₂ ] / [NHCO] = 10, in the case of polydodecanamide (polyamide 12) / [CH ₂ ] / [NHCO] = 11, and an aliphatic polyamide having a ratio of the number of methylene groups to the number of amide groups of 5 or more. In addition, the saturated water absorption of polycaproamide (polyamide 6) is 10.6%, the saturated water absorption of polyhexamethylene adipamide (polyamide 66) is 9.3%, and polyhexamethylene sebacamide (polyamide 610). The saturated water absorption is 3.0%, the saturated water absorption of polyhexamethylene dodecamide (polyamide 612) is 2.5%, the saturated water absorption of polydecamethylene sebacamide (polyamide 1010) is 2.2%, The saturated water absorption of methylenedodecanamide (polyamide 1012) is 2.0%, the saturated water absorption of polydodecane methylenedodecanamide (polyamide 1212) is 1.5%, and the saturated water absorption of polyundecanamide (polyamide 11) is 2. 0%, the saturated water absorption rate of polydodecanamide (polyamide 12) is 1.6%, and all of them have a saturated water absorption rate of 1.4% or more at 23 ° C in water. An aliphatic polyamide.

  The polyamide (A) may be a mixture of the above homopolymers, a mixture of the above copolymers, a mixture of a homopolymer and a copolymer, or another polyamide resin or other heat. It may be a mixture with a plastic resin. The content of the polyamide (A) is preferably 60% by mass or more, and more preferably 80% by mass or more.

  Other polyamide resins include polymetaxylylene adipamide (polyamide MXD6), polymetaxylylene veramide (polyamide MXD8), polymetaxylylene azelamide (polyamide MXD9), polymetaxylylene sebacamide (polyamide MXD10). , Polymetaxylylene decanamide (polyamide MXD12), polymetaxylylene terephthalamide (polyamide MXDT), polymetaxylylene isophthalamide (polyamide MXDI), polymetaxylylene naphthalamide (polyamide MXDN), polybis (4-aminocyclohexyl) Methanedecamide (Polyamide PACM12), Polybis (4-aminocyclohexyl) methane terephthalamide (Polyamide PACMT), Polybis (4-aminocyclohexyl) methane Phthalamide (polyamide PACMI), polybis (3-methyl-4-aminocyclohexyl) methane dodecamide (polyamide dimethyl PACM12), polyisophorone adipamide (polyamide IPD6), polyisophorone terephthalamide (polyamide IPDT), polyhexamethylene terephthalate Amide (polyamide 6T), polyhexamethylene isophthalamide (polyamide 6I), polytrimethylhexamethylene terephthalamide (polyamide TMHT), polynonamethylene terephthalamide (polyamide 9T), polynonamethylene isophthalamide (polyamide 9I) Polynonamethylene naphthalamide (polyamide 9N), Polynonamethylene hexahydroterephthalamide (polyamide 9T (H)), Polydecamethylene terephthalamide (Polyamide) Polydecamethylene isophthalamide (polyamide 10I), polydecamethylene naphthalamide (polyamide 10N), polydecamethylenehexahydroterephthalamide (polyamide 10T (H)), polyundecamethylene terephthalamide (polyamide 10T) Polyamide 11T), polyundecamethylene isophthalamide (polyamide 11I), polyundecamethylene naphthalamide (polyamide 11N), polyundecamethylenehexahydroterephthalamide (polyamide 11T (H)), polydodecamethylene terephthalate Lamidamide (polyamide 12T), polydodecamethylene isophthalamide (polyamide 12I), polydodecamethylene naphthalamide (polyamide 12N), polydodecamethylenehexahydroterephthalamide (polyamide 12T (H)) and these poly Examples include amide raw material monomers and / or copolymers using the above-mentioned polyamide (A) raw material monomers. These can use 1 type (s) or 2 or more types.

  Other thermoplastic resins to be mixed include high density polyethylene (HDPE), medium density polyethylene (MDPE), low density polyethylene (LDPE), linear low density polyethylene (LLDPE), and ultra high molecular weight polyethylene (UHMWPE). , Polypropylene (PP), ethylene / propylene copolymer (EPR), ethylene / butene copolymer (EBR), ethylene / vinyl acetate copolymer (EVA), saponified ethylene / vinyl acetate copolymer (EVOH), Ethylene / acrylic acid copolymer (EAA), ethylene / methacrylic acid copolymer (EMAA), ethylene / methyl acrylate copolymer (EMA), ethylene / methyl methacrylate copolymer (EMMA), ethylene / acrylic acid Polyolefin resins such as ethyl copolymer (EEA) and Polyolefin resin containing a functional group such as a boxyl group and a salt thereof, an acid anhydride group, and an epoxy group, polybutylene terephthalate (PBT), polyethylene terephthalate (PET), polyethylene isophthalate (PEI), Polymers, Polyarylate (PAR), Polyethylene naphthalate (PEN), Polybutylene naphthalate (PBN), Polyester resins such as liquid crystal polyester (LCP), Polyacetal (POM), Polyphenylene oxide (PPO) Resins, polysulfone resins such as polysulfone (PSF) and polyethersulfone (PES), polythioether resins such as polyphenylene sulfide (PPS) and polythioethersulfone (PTES), polyetheretherketone PEEK), polyketone resins such as polyallyl ether ketone (PAEK), polyacrylonitrile (PAN), polymethacrylonitrile, acrylonitrile / styrene copolymer (AS), methacrylonitrile / styrene copolymer, acrylonitrile / butadiene / Polystyrene resins such as styrene copolymer (ABS), methacrylonitrile / styrene / butadiene copolymer (MBS), polymethacrylate resins such as polymethyl methacrylate (PMMA), polyethyl methacrylate (PEMA), polyvinyl Polyvinyl resins such as alcohol (PVA), polyvinylidene chloride (PVDC), polyvinyl chloride (PVC), vinyl chloride / vinylidene chloride copolymer, vinylidene chloride / methyl acrylate copolymer, cellulose acetate, cellulose butyrate Cellulosic resins such as polyvinylidene fluoride (PVDF), polyvinyl fluoride (PVF), polychlorofluoroethylene (PCTFE), tetrafluoroethylene / ethylene copolymer (ETFE), ethylene / chlorotrifluoroethylene copolymer (ECTFE), tetrafluoroethylene / hexafluoropropylene copolymer (TFE / HFP, FEP), tetrafluoroethylene / hexafluoropropylene / vinylidene fluoride copolymer (TFE / HFP / VDF, THV), tetrafluoroethylene / Fluorine resin such as perfluoro (alkyl vinyl ether) copolymer (PFA), polycarbonate resin such as polycarbonate (PC), thermoplastic polyimide (PI), polyamideimide (PAI), polyetherimide Polyimide resins, thermoplastic polyurethane resins, polyurethane elastomers, polyester elastomers. These can use 1 type (s) or 2 or more types.

  Polyamide (A) production equipment includes batch-type reaction kettles, one-tank or multi-tank continuous reaction equipment, tubular continuous reaction equipment, single-screw kneading extruder, twin-screw kneading extruder, etc. For example, a known polyamide production apparatus can be used. Examples of the polymerization method include known methods such as melt polymerization, solution polymerization, and solid phase polymerization, and the polymerization can be performed by repeating normal pressure, reduced pressure, and pressure operations. These polymerization methods can be used alone or in appropriate combination.

  Moreover, it is preferable that it is 1.5-5.0, and, as for the relative viscosity measured based on JISK-6920 of polyamide (A), it is more preferable that it is 2.0-4.5. When the relative viscosity is less than the above value, the mechanical properties of the obtained laminated tube may be insufficient. May be difficult.

  The terminal amino group concentration [A] (μeq / g) and the terminal carboxyl group concentration [B] (μeq / g) per 1 g of the polyamide (A) satisfy [A]> [B] +5 (hereinafter referred to as terminal). It may be referred to as a modified aliphatic polyamide.) In view of compatibility with the polyamide (B) and polycarbonate, and more preferably [A]> [B] +10, and [A]> [B]. More preferably, it is +15. Furthermore, [A]> 20 is preferable, and 30 <[A] <120 is more preferable from the viewpoint of the melt stability of the polyamide and the suppression of the generation of the gel-like material.

  The terminal amino group concentration [A] (μeq / g) can be measured by dissolving the polyamide in a phenol / methanol mixed solution and titrating with 0.05N hydrochloric acid. The terminal carboxyl group concentration [B] (μeq / g) can be measured by dissolving the polyamide in benzyl alcohol and titrating with 0.05N sodium hydroxide solution.

  The terminal-modified aliphatic polyamide is produced by polymerizing or copolymerizing the raw material of the polyamide (A) in the presence of amines by a known method such as melt polymerization, solution polymerization or solid phase polymerization. Alternatively, it is produced by melt-kneading in the presence of amines after polymerization. Thus, amines can be added at any stage during polymerization, or after polymerization, at any stage during melt-kneading, but considering the durability of interlayer adhesion strength in a high-temperature atmosphere of the laminated tube, It is preferable to add at the stage of polymerization.

  Examples of the amines include monoamines, diamines, triamines, and polyamines. In addition to amines, carboxylic acids such as monocarboxylic acids, dicarboxylic acids, and tricarboxylic acids may be added as necessary as long as they do not deviate from the range of the above-mentioned end group concentration conditions. These amines and carboxylic acids may be added simultaneously or separately. In addition, the following exemplified amines and carboxylic acids can be used alone or in combination of two or more.

  Specific examples of the monoamine to be added include methylamine, ethylamine, propylamine, butylamine, pentylamine, hexylamine, heptylamine, octylamine, 2-ethylhexylamine, nonylamine, decylamine, undecylamine, dodecylamine, tridecylamine Aliphatic monoamines such as tetradecylamine, pentadecylamine, hexadecylamine, octadecylamine, octadecyleneamine, eicosylamine and docosylamine, alicyclic monoamines such as cyclohexylamine and methylcyclohexylamine, benzylamine, β- Aromatic monoamines such as phenylmethylamine, N, N-dimethylamine, N, N-diethylamine, N, N-dipropylamine, N, N-dibutylamine, N, N-dihexyl Symmetrical secondary amines such as amine, N, N-dioctylamine, N-methyl-N-ethylamine, N-methyl-N-butylamine, N-methyl-N-dodecylamine, N-methyl-N-octadecylamine, N -Hybrid secondary amines such as -ethyl-N-hexadecylamine, N-ethyl-N-octadecylamine, N-propyl-N-hexadecylamine, N-propyl-N-benzylamine and the like. These can use 1 type (s) or 2 or more types.

  Specific examples of the diamine to be added include 1,2-ethanediamine, 1,3-propanediamine, 1,4-butanediamine, 1,5-pentanediamine, 1,6-hexanediamine, and 1,7-heptanediamine. 1,8-octanediamine, 1,9-nonanediamine, 1,10-decanediamine, 1,11-undecanediamine, 1,12-dodecanediamine, 1,13-tridecanediamine, 1,14-tetradecanediamine, 1,15-pentadecanediamine, 1,16-hexadecanediamine, 1,17-heptadecanediamine, 1,18-octadecanediamine, 2- / 3-methyl-1,5-pentanediamine, 2-methyl-1,8 -Octanediamine, 2,2,4- / 2,4,4-trimethyl-1,6-hexanediamine, 5-methyl Aliphatic diamines such as 1,9-nonanediamine, 1,3- / 1,4-cyclohexanedimethylamine, bis (4-aminocyclohexyl) methane, bis (4-aminocyclohexyl) propane, bis (3-methyl-4- Aminocyclohexyl) methane, bis (3-methyl-4-aminocyclohexyl) propane, 5-amino-2,2,4-trimethyl-1-cyclopentanemethylamine, 5-amino-1,3,3-trimethylcyclohexanemethyl Examples thereof include alicyclic diamines such as amine, bis (aminopropyl) piperazine, bis (aminoethyl) piperazine, norbornane dimethylamine, and tricyclodecanedimethylamine, and aromatic diamines such as m- / p-xylylenediamine. These can use 1 type (s) or 2 or more types.

  Specific examples of the triamine to be added include 1,2,3-triaminopropane, 1,2,3-triamino-2-methylpropane, 1,2,4-triaminobutane, 1,2,3,4- Tetraminobutane, 1,3,5- / 1,2,4- / 1,2,3-triaminocyclohexane, 1,2,4,5-tetraminocyclohexane, 1,3,5- / 1,2,4 -/ 1,2,3-triaminobenzene, 1,2,4,5-tetraminobenzene, 1,2,4- / 2,5,7-triaminonaphthalene, 2,4,6-triaminopyridine, 1,2,7,8- / 1,4,5,8-tetraminonaphthalene and the like. These can use 1 type (s) or 2 or more types.

The polyamine to be added may be a compound having a plurality of primary amino groups (—NH ₂ ) and / or secondary amino groups (—NH—). For example, polyalkyleneimine, polyalkylenepolyamine, polyvinylamine, polyallylamine, etc. Is mentioned. The amino group with active hydrogen is the reaction point of the polyamine.

  The polyalkyleneimine is produced by a method of ionic polymerization of an alkyleneimine such as ethyleneimine or propyleneimine, or a method of polymerizing an alkyloxazoline and then partially hydrolyzing or completely hydrolyzing the polymer. Examples of the polyalkylene polyamine include diethylenetriamine, triethylenetetramine, pentaethylenehexamine, or a reaction product of ethylenediamine and a polyfunctional compound. Polyvinylamine can be obtained, for example, by polymerizing N-vinylformamide to poly (N-vinylformamide), and then partially or completely hydrolyzing the polymer with an acid such as hydrochloric acid. Polyallylamine is generally obtained by polymerizing a hydrochloride of an allylamine monomer and then removing hydrochloric acid. These can use 1 type (s) or 2 or more types. Among these, polyalkyleneimine is preferable.

  Examples of the polyalkyleneimine include one or more kinds of alkyleneimines having 2 to 8 carbon atoms such as ethyleneimine, propyleneimine, 1,2-butyleneimine, 2,3-butyleneimine, and 1,1-dimethylethyleneimine. The homopolymer and copolymer obtained by superposing | polymerizing by a conventional method are mentioned. Among these, polyethyleneimine is more preferable. A polyalkyleneimine is obtained by polymerizing an alkyleneimine as a raw material and using a branched polyalkyleneimine containing a primary amine, a secondary amine or a tertiary amine obtained by ring-opening polymerization of the alkyleneimine or an alkyloxazoline as a raw material. Either a linear polyalkyleneimine containing only a primary amine and a secondary amine, or a three-dimensionally crosslinked structure may be used. Furthermore, ethylenediamine, propylenediamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, dipropylenetriamine, tripropylenetetramine, dihexamethylenetriamine, aminopropylethylenediamine, bisaminopropylethylenediamine and the like may be included. A polyalkyleneimine is usually derived from the reactivity of an active hydrogen atom on a nitrogen atom contained therein, and in addition to a tertiary amino group, a primary amino group having an active hydrogen atom or a secondary amino group (imino Group).

  The number of nitrogen atoms in the polyalkyleneimine is not particularly limited, but is preferably 4 to 3,000, more preferably 8 to 1,500, and still more preferably 11 to 500. The number average molecular weight of the polyalkyleneimine is preferably from 100 to 20,000, more preferably from 200 to 10,000, and further preferably from 500 to 8,000.

  On the other hand, as carboxylic acids to be added, acetic acid, propionic acid, butyric acid, valeric acid, caproic acid, enanthic acid, caprylic acid, capric acid, pelargonic acid, undecanoic acid, lauric acid, tridecanoic acid, myristic acid, myristic acid, Aliphatic monocarboxylic acids such as palmitic acid, stearic acid, oleic acid, linoleic acid, arachidic acid, behenic acid, erucic acid, alicyclic monocarboxylic acids such as cyclohexanecarboxylic acid, methylcyclohexanecarboxylic acid, benzoic acid, toluic acid , Aromatic monocarboxylic acids such as ethylbenzoic acid, phenylacetic acid, malonic acid, succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, undecanedioic acid, dodecanedioic acid, hexadecanedioic acid , Hexadecenedioic acid, octadecadioic acid, octadecenedioic acid, ray Sandicarboxylic acid, eicosene dicarboxylic acid, docosanedicarboxylic acid, diglycolic acid, aliphatic dicarboxylic acids such as 2,2,4- / 2,4,4-trimethyladipic acid, 1,3- / 1,4- Cyclohexane dicarboxylic acid, cycloaliphatic dicarboxylic acid such as norbornane dicarboxylic acid, terephthalic acid, isophthalic acid, phthalic acid, m- / p-xylylene dicarboxylic acid, 1,4- / 2,6- / 2,7-naphthalenedicarboxylic acid Aromatic dicarboxylic acids such as acids, 1,2,4-butanetricarboxylic acid, 1,3,5-pentanetricarboxylic acid, 1,2,6- / 1,3,6-hexanetricarboxylic acid, 1,3,5 -Tricarboxylic acids such as cyclohexanetricarboxylic acid and trimesic acid. These can use 1 type (s) or 2 or more types.

  The amount of amine to be added is appropriately determined by a known method in consideration of the terminal amino group concentration, terminal carboxyl group concentration and relative viscosity of the terminal-modified aliphatic polyamide to be produced. Usually, the addition amount of amines is preferably 0.5 to 20 meq / mol, and 1.0 to 10 meq / mol with respect to 1 mol of the polyamide raw material (monomer constituting the repeating unit or 1 mol of the monomer unit). (Equivalent (eq) of amino group is defined as 1 equivalent of the amount of amino group that reacts 1: 1 with a carboxyl group to form an amide group). If the amount of amine added is less than the above value, sufficient reactivity may not be obtained, while if it exceeds the above value, it may be difficult to produce a polyamide having a desired viscosity. is there.

  In the terminal-modified aliphatic polyamide, it is preferable to add a diamine and / or a polyamine during polymerization in order to satisfy the condition of the terminal group concentration among the above-exemplified amines. More preferably, it is at least one selected from the group consisting of alicyclic diamine and polyamine.

  The terminal-modified aliphatic polyamide may be a mixture of two or more kinds of polyamides having different terminal group concentrations as long as the terminal group concentration is satisfied. In this case, the terminal amino group concentration and the terminal group carboxyl concentration of the polyamide mixture are determined by the terminal amino group concentration, the terminal carboxyl group concentration and the blending ratio of the polyamide constituting the mixture.

  Moreover, it is preferable to add a plasticizer to polyamide (A). Examples of the plasticizer include benzenesulfonic acid alkylamides, toluenesulfonic acid alkylamides, and hydroxybenzoic acid alkyl esters.

  Examples of benzenesulfonic acid alkylamides include benzenesulfonic acid propylamide, benzenesulfonic acid butyramide, and benzenesulfonic acid 2-ethylhexylamide. Examples of toluenesulfonic acid alkylamides include N-ethyl-o- / N-ethyl-p-toluenesulfonic acid butyramide, N-ethyl-o- / N-ethyl-p-toluenesulfonic acid 2-ethylhexylamide, and the like. It is done. Examples of hydroxybenzoic acid alkyl esters include ethylhexyl o- / p-hydroxybenzoate, hexyldecyl o- / p-hydroxybenzoate, ethyldecyl o- / p-hydroxybenzoate, octyloctyl o- / p-hydroxybenzoate Decyldodecyl o- / p-hydroxybenzoate, methyl o- / p-hydroxybenzoate, butyl o- / p-hydroxybenzoate, hexyl o- / p-hydroxybenzoate, o- / p-hydroxybenzoic acid n-octyl, o- / p-hydroxybenzoic acid decyl, o- / p-hydroxybenzoic acid dodecyl and the like. These can use 1 type (s) or 2 or more types.

  Among these, benzenesulfonic acid alkylamides such as benzenesulfonic acid butyramide and benzenesulfonic acid 2-ethylhexylamide, N-ethyl-p-toluenesulfonic acid butyramide, N-ethyl-p-toluenesulfonic acid 2-ethylhexylamide and the like Preferred are hydroxybenzoic acid alkyl esters such as toluenesulfonic acid alkylamides, p-hydroxybenzoic acid ethylhexyl, p-hydroxybenzoic acid hexyldecyl, p-hydroxybenzoic acid ethyldecyl, benzenesulfonic acid butyramide, p-hydroxybenzoic acid More preferred is ethylhexyl and / or hexyldecyl p-hydroxybenzoate.

  The compounding amount of the plasticizer is preferably 1 to 30 parts by mass and more preferably 1 to 15 parts by mass with respect to 100 parts by mass of the polyamide (A). When the blending amount of the plasticizer exceeds the above value, the low temperature impact resistance of the laminated tube may be lowered.

  Moreover, it is preferable to add an impact resistance improving material to the polyamide (A). Examples of the impact resistance improving material include rubbery polymers, and the flexural modulus measured in accordance with ASTM D-790 is preferably 500 MPa or less. If the flexural modulus exceeds this value, the impact improvement effect may be insufficient.

  Examples of the impact resistance improver include a copolymer containing an α-olefin and ethylene and / or propylene, a copolymer containing ethylene and / or propylene and an α, β-unsaturated carboxylic acid and / or an unsaturated carboxylic acid ester, Examples thereof include a copolymer containing an aromatic vinyl compound and a conjugated diene compound, and an ionomer polymer, and these may be used alone or in combination of two or more.

  The copolymer containing the α-olefin and ethylene and / or propylene is a polymer obtained by copolymerizing ethylene and / or propylene and an α-olefin having 3 or more carbon atoms, and as an α-olefin having 3 or more carbon atoms. Are propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, 1-nonene, 1-decene, 1-undecene, 1-dodecene, 1-tridecene, 1-tetradecene, 1- Pentadecene, 1-hexadecene, 1-heptadecene, 1-octadecene, 1-nonadecene, 1-eicosene, 3-methyl-1-butene, 3-methyl-1-pentene, 3-ethyl-1-pentene, 4-methyl- 1-pentene, 4-methyl-1-hexene, 4,4-dimethyl-1-hexene, 4,4-dimethyl-1-pentene, 4-ethyl-1 Hexene, 3-ethyl-1-hexene, 9-methyl-1-decene, 11-methyl-1-dodecene, 12-ethyl-1-tetradecene, and the like. These can use 1 type (s) or 2 or more types. In addition, 1,4-pentadiene, 1,4- / 1,5-hexadiene, 1,4- / 1,5- / 1,6- / 1,7-octadiene, 2-methyl-1,5-hexadiene, 6-methyl-1,5-heptadiene, 7-methyl-1,6-octadiene, 4-ethylidene-8-methyl-1,7-nonadiene, 4,8-dimethyl-1,4,8-decatriene (DMDT) , Dicyclopentadiene, cyclohexadiene, cyclooctadiene, 5-vinylnorbornene, 5-ethylidene-2-norbornene, 5-methylene-2-norbornene, 5-isopropylidene-2-norbornene, 6-chloromethyl-5-iso Propenyl-2-norbornene, 2,3-diisopropylidene-5-norbornene, 2-ethylidene-3-isopropylidene-5-norbornene The non-conjugated diene polyene such as 2-propenyl-2,5-norbornadiene may be copolymerized. These can use 1 type (s) or 2 or more types.

  The above copolymer containing ethylene and / or propylene and α, β-unsaturated carboxylic acid and / or unsaturated carboxylic acid ester is ethylene and / or propylene and α, β-unsaturated carboxylic acid and / or unsaturated. It is a polymer obtained by copolymerizing a carboxylic acid ester monomer, and examples of the α, β-unsaturated carboxylic acid monomer include acrylic acid and methacrylic acid, and an α, β-unsaturated carboxylic acid ester monomer. Examples of the unsaturated carboxylic acid include methyl ester, ethyl ester, propyl ester, butyl ester, pentyl ester, hexyl ester, heptyl ester, octyl ester, nonyl ester, and decyl ester. These can use 1 type (s) or 2 or more types.

  The copolymer containing an aromatic vinyl compound and a conjugated diene compound is a block copolymer comprising an aromatic vinyl compound polymer block and a conjugated diene compound polymer block, and the aromatic vinyl compound polymer block. And a block copolymer having at least one conjugated diene compound-based polymer block. In the block copolymer, the unsaturated bond in the conjugated diene compound-based polymer block may be hydrogenated.

  The aromatic vinyl compound polymer block is a polymer block mainly composed of units derived from an aromatic vinyl compound. In this case, the aromatic vinyl compound includes styrene, o- / m- / p-methylstyrene, 1,5- / 2,4-dimethylstyrene, vinylnaphthalene, vinylanthracene, 4-propylstyrene, 4-cyclohexylstyrene. , 4-dodecylstyrene, 2-ethyl-4-benzylstyrene, 4- (phenylbutyl) styrene, and the like, and one or more of them can be used. In addition, the aromatic vinyl compound-based polymer block may optionally have a unit composed of a small amount of another unsaturated monomer.

  Conjugated diene compound-based polymer blocks are 1,3-butadiene, chloroprene, isoprene, 2,3-dimethyl-1,3-butadiene, 1,3-pentadiene, 4-methyl-1,3-pentadiene, 1,3 -A polymer block formed from one or more conjugated diene compounds such as hexadiene, and a copolymer containing a hydrogenated aromatic vinyl compound and a conjugated diene compound, part of the unsaturated bond Or all are saturated bonds.

  The molecular structure of the block copolymer including the aromatic vinyl compound and the conjugated diene compound and the hydrogenated product thereof may be any of linear, branched, radial, or any combination thereof. Among these, as a copolymer containing an aromatic vinyl compound and a conjugated diene compound and / or a hydrogenated product thereof, one aromatic vinyl compound polymer block and one conjugated diene compound polymer block are linear. The three polymer blocks are bonded in a straight chain in the order of diblock copolymer, aromatic vinyl compound polymer block, conjugated diene compound polymer block, and aromatic vinyl compound polymer block. One or more of these triblock copolymers and hydrogenated products thereof are preferably used. Unhydrogenated or hydrogenated styrene / butadiene block copolymers, unhydrogenated or hydrogenated styrene / isoprene block copolymers Polymer, unhydrogenated or hydrogenated styrene / isoprene / styrene block copolymer, unhydrogenated or hydrogenated styrene / butadiene / styrene block Copolymers, non-hydrogenated or include hydrogenated styrene / (isoprene / butadiene) / styrene block copolymer.

  The ionomer polymer is obtained by ionizing at least part of the carboxyl group of a copolymer containing an olefin and an α, β-unsaturated carboxylic acid by neutralization of metal ions. Ethylene is preferably used as the olefin, and acrylic acid and methacrylic acid are preferably used as the α, β-unsaturated carboxylic acid, but are not limited to those exemplified here, The body may be copolymerized. Metal ions include alkali metals such as Li, Na, K, Mg, Ca, Sr, Ba, alkaline earth metals, Al, Sn, Sb, Ti, Mn, Fe, Ni, Cu, Zn, Cd, etc. Is mentioned. These can use 1 type (s) or 2 or more types.

  Further, a copolymer containing an α-olefin and ethylene and / or propylene used as an impact resistance improver, a copolymer containing ethylene and / or propylene and an α, β-unsaturated carboxylic acid and / or unsaturated carboxylic acid ester As the copolymer containing a polymer, an aromatic vinyl compound and a conjugated diene compound, a polymer modified with a carboxylic acid and / or a derivative thereof is preferably used. By modifying with such a component, a functional group having affinity for the polyamide (A) is contained in the molecule.

  Examples of the functional group having affinity for the polyamide (A) include a carboxyl group, an acid anhydride group, a carboxylic acid ester group, a carboxylic acid metal salt, a carboxylic acid imide group, a carboxylic acid amide group, and an epoxy group. . Examples of compounds containing these functional groups include acrylic acid, methacrylic acid, maleic acid, fumaric acid, itaconic acid, crotonic acid, mesaconic acid, citraconic acid, glutaconic acid, cis-4-cyclohexene-1,2-dicarboxylic acid Acid, endobicyclo- [2.2.1] -5-heptene-2,3-dicarboxylic acid and metal salts of these carboxylic acids, monomethyl maleate, monomethyl itaconate, methyl acrylate, ethyl acrylate, butyl acrylate 2-ethylhexyl acrylate, hydroxyethyl acrylate, methyl methacrylate, 2-ethylhexyl methacrylate, hydroxyethyl methacrylate, aminoethyl methacrylate, dimethyl maleate, dimethyl itaconate, maleic anhydride, itaconic anhydride, citracone anhydride Acid, endobicyclo- 2.2.1] -5-heptene-2,3-dicarboxylic anhydride, maleimide, N-ethylmaleimide, N-butylmaleimide, N-phenylmaleimide, acrylamide, methacrylamide, glycidyl acrylate, glycidyl methacrylate, Examples include glycidyl ethacrylate, glycidyl itaconate, and glycidyl citraconic acid. These can use 1 type (s) or 2 or more types.

  The blending amount of the impact resistance improving material is preferably 1 to 35 parts by mass and more preferably 5 to 25 parts by mass with respect to 100 parts by mass of the polyamide (A). When the blending amount of the impact resistance improving material exceeds the above value, the original mechanical properties of the laminated tube may be impaired.

  Furthermore, for the polyamide (A), if necessary, an antioxidant, a heat stabilizer, an ultraviolet absorber, a light stabilizer, a lubricant, an inorganic filler, an antistatic agent, a flame retardant, a crystallization accelerator, a coloring agent. An agent or the like may be added.

[Polyamide (B)]
The polyamide (B) used in the present invention comprises diamine units containing 50 mol% or more of aliphatic diamine units having 9 to 13 carbon atoms with respect to all diamine units, and oxalic acid units with respect to all dicarboxylic acid units. It is a polyamide comprising dicarboxylic acid units containing 60 mol% or more.

  The content of oxalic acid units in the polyamide (B) is 60 mol% or more, preferably 70 mol% or more, more preferably 80 mol% or more, based on all dicarboxylic acid units. When the content of the oxalic acid unit is less than the above value, various physical properties such as heat resistance, chemical resistance and chemical solution permeation prevention property of the obtained laminated tube tend to be lowered.

Examples of oxalic acid units include units derived from oxalic acid or its ester-forming derivatives. Units derived from ester-forming derivatives include aliphatic monohydric alcohols such as dimethyl oxalate, diethyl oxalate, di-n- (or i-) propyl oxalate, di-n- (or i-, or t-) butyl oxalate And units derived from aromatic alcohols such as oxalic acid diesters of alicyclic alcohols such as dicyclohexyl oxalate and diphenyl oxalate. These can use 1 type (s) or 2 or more types. Among these, a unit derived from an oxalic acid diester of an aliphatic monohydric alcohol having 3 or more carbon atoms, an oxalic acid diester of an alicyclic alcohol, or an oxalic acid diester of an aromatic alcohol, and preferably dibutyl oxalate and / or More preferred are units derived from diphenyl oxalate.
The polyamide (B) is a diamine unit containing 50 mol% or more of an aliphatic diamine unit having 9 to 13 carbon atoms based on all diamine units, and a dicarboxylic acid containing 60 mol% or more oxalic acid units based on all dicarboxylic acid units. A polyamide mainly composed of an aliphatic structure composed of acid units. For example, the number of methylene groups ([CH ₂ ]) and the number of amide groups of a polyamide composed of dibutyl oxalate as oxalic acid units and aliphatic diamine having 10 carbon atoms as diamine units The ratio ([CH ₂ ] / [NHCO]) of ([NHCO]) is 5. However, as a notable performance derived from the oxamide bond, polyamide (B) has low water absorption, for example, polynonamethylene oxamide (polyamide 92) has a saturated water absorption of 1.3%, polydeca The saturated water absorption of methylene oxamide (polyamide 102) is 1.0%, and the saturated water absorption of polydodecamethylene oxamide (polyamide 122) is 0.8%. Therefore, the polyamide (B) is clearly distinguished from the polyamide (A).

  The dicarboxylic acid unit in the polyamide (B) may contain other dicarboxylic acid units other than the unit derived from oxalic acid, as long as the excellent properties of the laminated tube of the present invention are not impaired. Other dicarboxylic acid units include malonic acid, dimethylmalonic acid, succinic acid, glutaric acid, adipic acid, 2-methyladipic acid, 2,2,4- / 2,4,4-trimethyladipic acid, pimelic acid, 2,2-dimethylglutaric acid, 2,2-diethylsuccinic acid, suberic acid, azelaic acid, sebacic acid, undecanedicarboxylic acid, dodecanedicarboxylic acid and other aliphatic dicarboxylic acids, 1,3-cyclopentanedicarboxylic acid, 1, Alicyclic dicarboxylic acids such as 3- / 1,4-cyclohexanedicarboxylic acid, phthalic acid, terephthalic acid, isophthalic acid, 1,3- / 1,4-phenylenedioxydiacetic acid, 2,6- / 2,7 -/ 1,4- / 1,5-naphthalenedicarboxylic acid, anthracene dicarboxylic acid, 4,4'-oxydibenzoic acid, 4,4'-diphenyldicarboxylic acid , Diphenylmethane-4,4′-dicarboxylic acid, diphenylethane-4,4′-dicarboxylic acid, diphenylpropane-4,4′-dicarboxylic acid, diphenyl ether-4,4′-dicarboxylic acid, diphenylsulfone-4,4 ′ -Units derived from aromatic dicarboxylic acids such as -dicarboxylic acid and 4,4'-triphenyldicarboxylic acid can be mentioned, and these can be used alone or in combination of two or more. The content of other dicarboxylic acid units is 40 mol% or less, preferably 30 mol%, more preferably 20 mol% or less, and further preferably 15 mol% or less. Furthermore, polycarboxylic acids such as trimellitic acid, trimesic acid, and pyromellitic acid can be used within a range where melt molding is possible.

  Further, the content of the aliphatic diamine unit having 9 to 13 carbon atoms in the polyamide (B) is 50 mol% or more, preferably 55 mol% or more, preferably 60 mol% with respect to the total diamine units. More preferably. When the content of the aliphatic diamine unit having 9 to 13 carbon atoms is less than the above value, the heat resistance, chemical resistance, and impact resistance of the laminated tube tend to decrease.

  The aliphatic diamine unit having 9 to 13 carbon atoms is derived from 1,9-nonanediamine, 1,10-decanediamine, 1,11-undecanediamine, 1,12-dodecanediamine, and 1,13-tridecanediamine. Units. As long as the carbon number satisfies the above, 2,2,4- / 2,4,4-trimethyl-1,6-hexanediamine, 2,4-diethyl-1,6-hexanediamine, 2,2- / 2, 3- / 2,4- / 2,5-dimethyl-heptanediamine, 2- / 3- / 4-methyl-1,8-octanediamine, 1,3- / 1,4- / 2,2- / 2 , 4- / 3,3- / 3,4- / 4,4- / 4,5-dimethyl-1,8-octanediamine, 5-methyl-1,9-nonanediamine, 2- / 3-butyl-1 , Units derived from branched aliphatic diamines such as 8-octanediamine may be contained. These can use 1 type (s) or 2 or more types.

  Among the above aliphatic diamine units having 9 to 13 carbon atoms, 1,9-nonanediamine and / or 2-methyl- are excellent from the viewpoint of melt moldability and low water absorption, chemical resistance and hydrolysis resistance. Units derived from 1,8-octanediamine, 1,10-decanediamine and 1,12-dodecanediamine are preferred. Furthermore, the molar ratio of the 1,9-nonanediamine unit to the 2-methyl-1,8-octanediamine unit is 30:70 to 98: 2 mol% from the viewpoint of the balance between moldability and impact resistance. Preferably, it is 40: 60-95: 5 mol%.

  As long as the diamine unit in the polyamide (B) is within a range that does not impair the excellent properties of the laminated tube of the present invention, other diamine units other than units derived from aliphatic diamines having 9 to 13 carbon atoms are included. May be included. Other diamine units include 1,2-ethanediamine, 1,3-propanediamine, 1,4-butanediamine, 1,6-hexanediamine, 1,8-octanediamine, 1,14-tetradecanediamine, , 15-pentadecanediamine, 1,16-hexadecanediamine, 1,17-heptadecanediamine, 1,18-octadecanediamine, aliphatic diamine such as 2- / 3-methyl-1,5-pentanediamine, 1,3 -/ 1,4-cyclohexanediamine, 1,3- / 1,4-cyclohexanedimethylamine, bis (4-aminocyclohexyl) methane, bis (4-aminocyclohexyl) propane, bis (3-methyl-4-aminocyclohexyl) ) Methane, bis (3-methyl-4-aminocyclohexyl) propane, 5-amino-2 2,4-trimethyl-1-cyclopentanemethylamine, 5-amino-1,3,3-trimethylcyclohexanemethylamine, bis (aminopropyl) piperazine, bis (aminoethyl) piperazine, norbornanedimethylamine, tricyclodecanedimethyl Alicyclic diamines such as amines, m- / p-phenylenediamine, m- / p-xylylenediamine, 1,4- / 1,5- / 2,6- / 2,7-naphthalenedimethylamine, 4, Examples include units derived from aromatic diamines such as 4′-diaminodiphenylmethane, 2,2-bis (4-aminophenyl) propane, 4,4′-diaminodiphenylsulfone, and 4,4′-diaminodiphenyl ether. Can use 1 type (s) or 2 or more types. The content of other diamine units is 50 mol% or less, preferably 45 mol% or less, and more preferably 40 mol% or less.

  The polyamide (B) may contain other units other than the dicarboxylic acid unit and the diamine unit as long as the excellent properties of the laminated tube of the present invention are not impaired. Other units include caprolactam, enantolactam, undecane lactam, dodecane lactam, α-pyrrolidone, α-piperidone, 6-aminocaproic acid, 7-aminoheptanoic acid, 9-aminononanoic acid, 11-aminoundecanoic acid, 12-amino Examples include units derived from dodecanoic acid. These can use 1 type (s) or 2 or more types. The content of units other than dicarboxylic acid units and diamine units is preferably 30 mol% or less, and more preferably 10 mol% or less.

  The relative viscosity of the polyamide (B) measured according to JIS K-6920 is preferably 1.8 to 6.0, more preferably 2.0 to 5.5, and 2.5 to More preferably, it is 4.5. When the relative viscosity is less than the above value, the mechanical properties of the obtained laminated tube may be insufficient. May be difficult.

  Polyamide (B) production equipment includes batch-type reaction kettles, single-tank or multi-tank continuous reaction equipment, tubular continuous reaction equipment, single-screw kneading extruder, twin-screw kneading extruder, etc. For example, a known polyamide production apparatus can be used. Examples of the polymerization method include known methods such as melt polymerization, solution polymerization, and solid phase polymerization, and the polymerization can be performed by repeating normal pressure, reduced pressure, and pressure operation. These polymerization methods can be used alone or in appropriate combination. Specifically, it is preferable to carry out in the order of (i) pre-polycondensation step and (ii) post-polycondensation step as shown by the following operations.

(I) Pre-polycondensation step: First, the inside of the reactor is purged with nitrogen, and then the diamine and, for example, oxalic acid diester are mixed. When mixing, a solvent in which both the diamine and the oxalic acid diester are soluble may be used. The solvent in which both the diamine component and the oxalic acid diester are soluble is not particularly limited, and examples thereof include toluene, xylene, trichlorobenzene, phenol, trifluoroethanol and the like. Of these, toluene is preferred. For example, after heating the toluene solution which melt | dissolved diamine to 50 degreeC, oxalic acid diester is added with respect to this. At this time, the charging ratio of the oxalic acid diester and the diamine is oxalic acid diester / the diamine, and is usually 0.8 to 1.5 (molar ratio) and 0.91 to 1.1 (molar ratio). Preferably, it is 0.99 to 1.01 (molar ratio).
The temperature in the reactor charged in this way is increased under normal pressure while stirring and / or nitrogen bubbling. The final temperature reached in the prepolycondensation step is preferably 80 to 150 ° C, and more preferably 100 to 140 ° C. The reaction time at the final temperature reached is 3-6 hours.

  (Ii) Post-polycondensation step: In order to further increase the molecular weight, the polymer produced in the pre-polycondensation step is gradually heated in the reactor under normal pressure. From the final reached temperature in the pre-polycondensation step, that is, from 80 to 150 ° C. in the temperature raising process, the final reached temperature in the post-polycondensation step is preferably 220 to 300 ° C., more preferably 230 to 280 ° C. It is more preferable that it is 240-270 degreeC. The post-polymerization reaction time including the temperature raising time is preferably 1 to 8 hours, and more preferably 2 to 6 hours. Furthermore, in the post-polymerization step, polymerization can be performed under reduced pressure as necessary. When carrying out vacuum polymerization, the final ultimate pressure is preferably 13.3 Pa to 0.1 MPa.

  Hereinafter, the manufacturing method of polyamide (B) is demonstrated concretely. First, the raw material oxalic acid diester is charged into a container and purged with nitrogen. The container is not particularly limited as long as it can withstand the temperature and pressure of the polycondensation reaction to be performed later. Thereafter, the container is heated to a temperature at which it is mixed with the raw material diamine, and then the diamine is injected to start the polycondensation reaction. The temperature at which the raw materials are mixed is not particularly limited as long as the temperature is not lower than the melting point and lower than the boiling point of the raw oxalic acid diester and diamine, and the polyamide produced by the polycondensation reaction of the oxalic acid diester and diamine is not thermally decomposed. When the mixing temperature is equal to or higher than the boiling point of the alcohol produced by the condensation reaction, it is desirable to use a container equipped with a device for distilling and condensing the alcohol. In addition, when pressure polymerization is performed in the presence of an alcohol generated by a condensation reaction, a pressure vessel is used. The charging ratio of oxalic acid diester and diamine is oxalic acid diester / diamine, and is usually 0.8 to 1.2 (molar ratio), preferably 0.91 to 1.09 (molar ratio). It is more preferable that it is .98 to 1.02 (molar ratio).

  Next, the inside of the container is heated to a temperature not lower than the melting point of the polyamide and not higher than the temperature at which the pyrolysis does not occur. For example, a diamine and oxalic acid composed of 1,9-nonanediamine and 2-methyl-1,8-octanediamine, and the molar ratio of 1,9-nonanediamine and 2-methyl-1,8-octanediamine is 85:15 In the case of polyamide using dibutyl as a raw material, the melting point is 235 ° C., so it is preferable to raise the temperature to 240 to 280 ° C. (pressure is 2 to 4 MPa). While distilling off the produced alcohol, the polycondensation reaction is continued under an atmospheric pressure of nitrogen or reduced pressure as necessary. When raw materials are mixed in a pressure-resistant vessel and subjected to pressure polymerization in the presence of an alcohol produced by a condensation reaction, the pressure is first released while the produced alcohol is distilled off. Thereafter, the polycondensation reaction is continued under an atmospheric pressure of nitrogen or reduced pressure as necessary. When carrying out vacuum polymerization, the final ultimate pressure is preferably 13.3 Pa to 0.1 MPa. It is preferable that temperature is 240-280 degreeC. The alcohol is cooled and liquefied by a water-cooled condenser and recovered.

  Furthermore, the polyamide (B) may be added to an antioxidant, a heat stabilizer, an ultraviolet absorber, a light stabilizer, a lubricant, an inorganic filler, an antistatic agent, a flame retardant, a crystallization accelerator, a plasticizer, if necessary. Agents, colorants, lubricants, impact resistance improvers, other thermoplastic resins, and the like may be added. In order to improve the low temperature impact resistance of the polyamide (B), it is preferable to add an impact resistance improving material, and the flexural modulus measured in accordance with ASTM D-790 described in the description of the polyamide (A). It is more preferable to add a polymer having a viscosity of 500 MPa or less.

  The polyamide (B) may contain other polyamide-based resins or other thermoplastic resins. Examples of other polyamide-based resins or other thermoplastic resins include the same resins as in the case of polyamide (A). Further, it may be a mixture with polyamide (A). The content of other polyamide resins or other thermoplastic resins in the mixture is preferably 20% by mass or less.

  In order to improve long-term heat resistance, a polyamide compound can also be mix | blended with polyamide (B). Specific examples of the copper compound to be blended include cuprous chloride, cupric chloride, cuprous bromide, cupric bromide, cuprous iodide, cupric iodide, cupric sulfate. Copper, cupric nitrate, cupric phosphate, cupric pyrophosphate, cuprous acetate, cupric acetate, cupric salicylate, cupric stearate, cupric benzoate, inorganic halogenated Examples thereof include complex salts of copper with xylylenediamine, 2-mercaptobenzimidazole, 2-mercaptobenzthiazole, benzimidazole, and the like. These can use 1 type (s) or 2 or more types.

  The compounding amount of the copper compound is preferably 0.01 to 3 parts by mass and more preferably 0.02 to 1 part by mass with respect to 100 parts by mass of the polyamide (B). If the compounding amount of the copper compound is less than the above value, the heat resistance of the obtained laminated tube may not be sufficient, and if it exceeds the above value, liberation of the metal salt occurs during melt molding of the laminated tube, Coloring may impair the value of the product.

Moreover, it is also possible to add a halogenated alkali metal compound to the polyamide (B) in a form used in combination with the copper compound. Specific examples of the alkali metal halide include lithium chloride, lithium bromide, lithium iodide, lithium fluoride, sodium chloride, sodium bromide, sodium iodide, potassium chloride, potassium bromide, potassium iodide, Examples include potassium fluoride. These can use 1 type (s) or 2 or more types. Among these, potassium iodide is preferable. The compounding amount of the alkali metal halide compound is preferably 0.01 to 10 parts by mass, more preferably 0.02 to 3 parts by mass with respect to 100 parts by mass of the polyamide (B). The range of 100 to 1,000 parts by mass is more preferable with respect to 100 parts by mass of the copper compound.
Furthermore, it is also preferable to blend the copper compound and the alkali metal halide compound with respect to the polyamide (A) for the purpose of improving long-term heat resistance.

[Polyamide (C)]
The polyamide (C) of the present invention is a resin composition containing a polycarbonate relative to the polyamide (A) and the polyamide (B) (hereinafter sometimes referred to as polyoxamide).
The polycarbonate in the polyamide (C) may be a compound having at least two carbonate units, and a method of reacting a dihydroxy compound and phosgene in the presence of an aqueous sodium hydroxide solution and a methylene chloride solvent (interfacial polymerization method, phosgene method). Or a method produced by a known method such as a method of transesterifying a dihydroxy compound and a carbonic acid diester in a molten state or a solid phase (melting method, solid phase method) can be used.

  As a dihydroxy compound, an aromatic dihydroxy compound, an aliphatic dihydroxy compound, etc. are mentioned, for example, As an aromatic dihydroxy compound, the compound shown by following General formula (1) is mentioned.

上記一般式（Ｉ）において、Ｒ^３及びＲ^４は、それぞれフッ素、塩素、臭素、ヨウ素のハロゲン原子又は炭素数１〜８のアルキル基、例えばメチル基、エチル基、ｎ−プロピル基、イソプロピル基、ｎ−ブチル基、イソブチル基、ｓｅｃ−ブチル基、ｔ−ブチル基、ペンチル基、ヘキシル基、シクロヘキシル基、ヘプチル基、オクチル基等を示す。Ｒ^３及びＲ^４は互いに同一であっても異なっていてもよい。また、Ｒ^３が複数ある場合は複数のＲ^３は同一でも異なっていてもよく、Ｒ^４が複数ある場合は複数のＲ^４は同一でも異なっていてもよい。ｍ及びｎは、それぞれ０〜４の整数である。そして、Ｚは単結合、炭素数１〜８のアルキレン基、炭素数２〜８のアルキリデン基、炭素数５〜１５のシクロアルキレン基、炭素数５〜１５のシクロアルキリデン基、又は−Ｓ−、−ＳＯ−、−ＳＯ２−、−Ｏ−、−ＣＯ−結合若しくは式（ＩＩ）、（ＩＩ’）

In the above general formula (I), R ³ and R ⁴ are each a halogen atom of fluorine, chlorine, bromine or iodine or an alkyl group having 1 to 8 carbon atoms, such as a methyl group, an ethyl group, an n-propyl group, or an isopropyl group. N-butyl group, isobutyl group, sec-butyl group, t-butyl group, pentyl group, hexyl group, cyclohexyl group, heptyl group, octyl group and the like. R ³ and R ⁴ may be the same or different from each other. Also, it may be a plurality of R ³ when there are a plurality of R ³ are identical or different, a plurality of R ⁴ if R ⁴ there are a plurality may be the same or different. m and n are each an integer of 0 to 4. Z is a single bond, an alkylene group having 1 to 8 carbon atoms, an alkylidene group having 2 to 8 carbon atoms, a cycloalkylene group having 5 to 15 carbon atoms, a cycloalkylidene group having 5 to 15 carbon atoms, or -S-, -SO-, -SO2-, -O-, -CO- bond or formula (II), (II ')

で示される結合を示す。炭素数１〜８のアルキレン基、炭素数２〜８のアルキリデン基としては、例えばメチレン基、エチレン基、プロピレン基、ブチレン基、ペンチレン基、ヘキシレン基、エチリデン基、イソプロピリデン基等が挙げられ、炭素数５〜１５のシクロアルキレン基、炭素数５〜１５のシクロアルキリデン基としては、例えばシクロペンチレン基、シクロヘキシレン基、シクロペンチリデン基、シクロヘキシリデン基等が挙げられる。

The bond shown by is shown. Examples of the alkylene group having 1 to 8 carbon atoms and the alkylidene group having 2 to 8 carbon atoms include a methylene group, an ethylene group, a propylene group, a butylene group, a pentylene group, a hexylene group, an ethylidene group, and an isopropylidene group. Examples of the cycloalkylene group having 5 to 15 carbon atoms and the cycloalkylidene group having 5 to 15 carbon atoms include a cyclopentylene group, a cyclohexylene group, a cyclopentylidene group, and a cyclohexylidene group.

  Examples of the aromatic dihydroxy compound represented by the general formula (I) include bis (4-hydroxyphenyl) methane, bis (3-methyl-4-hydroxyphenyl) methane, and bis (3-chloro-4-hydroxy). Phenyl) methane, bis (3,5-dibromo-4-hydroxyphenyl) methane, 1,1-bis (4-hydroxyphenyl) ethane, 1,1-bis (2-tert-butyl-4-hydroxy-3-) Methylphenyl) ethane, 1,1-bis (2-tert-butyl-4-hydroxy-3-methylphenyl) ethane, 1-phenyl-1,1-bis (3-fluoro-4-hydroxy-3-methylphenyl) ) Ethane, 2,2-bis (4-hydroxyphenyl) propane (commonly called bisphenol A), 2,2-bis (3-methyl-4-hydroxyphenyl) propyl Bread, 2,2-bis (2-methyl-4-hydroxyphenyl) propane, 2,2-bis (3,5-dimethyl-4-hydroxyphenyl) propane, 1,1-bis (2-t-butyl-) 4-hydroxy-5-methylphenyl) propane, 2,2-bis (3-chloro-4-hydroxyphenyl) propane, 2,2-bis (3-fluoro-4-hydroxyphenyl) propane, 2,2-bis (3-bromo-4-hydroxyphenyl) propane, 2,2-bis (3,5-difluoro-4-hydroxyphenyl) propane, 2,2-bis (3,5-dichloro-4-hydroxyphenyl) propane, 2,2-bis (3,5-dibromo-4-hydroxyphenyl) propane, 2,2-bis (4-hydroxyphenyl) butane, 2,2-bis (4-hydroxy) Enyl) octane, 2,2-bis (4-hydroxyphenyl) phenylmethane, 2,2-bis (4-hydroxy-1-methylphenyl) propane, 1,1-bis (4-hydroxy-t-butylphenyl) Propane, 2,2-bis (4-hydroxy-3-bromophenyl) propane, 2,2-bis (4-hydroxy-3,5-dimethylphenyl) propane, 2,2-bis (4-hydroxy-3-) Chlorophenyl) propane, 2,2-bis (4-hydroxy-3,5-dichlorophenyl) propane, 2,2-bis (4-hydroxy-3,5-dibromophenyl) propane, 2,2-bis (3-bromo) -4-hydroxy-5-chlorophenyl) propane, 2,2-bis (3-phenyl-4-hydroxyphenyl) propane, 2,2-bis (4-hydride) Loxyphenyl) butane, 2,2-bis (3-methyl-4-hydroxyphenyl) butane, 1,1-bis (2-butyl-4-hydroxy-5-methylphenyl) butane, 1,1-bis (2 -T-butyl-4-hydroxy-5-methylphenyl) butane, 1,1-bis (2-t-butyl-4-hydroxy-5-methylphenyl) isobutane, 1,1-bis (2-t-amyl) -4-hydroxy-5-methylphenyl) butane, 2,2-bis (3,5-dichloro-4-hydroxyphenyl) butane, 2,2-bis (3,5-dibromo-4-hydroxyphenyl) butane, 4,4-bis (4-hydroxyphenyl) heptane, 1,1-bis (2-tert-butyl-4-hydroxy-5-methylphenyl) heptane, 2,2-bis (4-hydroxyphenyl) Bis (hydroxyaryl) alkanes such as octane, 1,1- (4-hydroxyphenyl) ethane, 1,1-bis (4-hydroxyphenyl) cyclopentane, 1,1-bis (4-hydroxyphenyl) cyclohexane, 1,1-bis (3-methyl-4-hydroxyphenyl) cyclohexane, 1,1-bis (3-cyclohexyl-4-hydroxyphenyl) cyclohexane, 1,1-bis (3-phenyl-4-hydroxyphenyl) cyclohexane 1,1-bis (4-hydroxyphenyl) -3,5,5-trimethylcyclohexane, bis (hydroxyaryl) cycloalkanes, bis (4-hydroxyphenyl) ether, bis (4-hydroxy-3-methyl) Bis (hydroxyaryl) ethers such as phenyl) ether, Bis (hydroxyaryl) sulfides such as bis (4-hydroxyphenyl) sulfide, bis (3-methyl-4-hydroxyphenyl) sulfide, bis (4-hydroxyphenyl) sulfoxide, bis (3-methyl-4-hydroxyphenyl) ) Bis (hydroxyaryl) sulfoxides such as sulfoxide, bis (3-phenyl-4-hydroxyphenyl) sulfoxide, bis (4hydroxyphenyl) sulfone, bis (3-methyl-4-hydroxyphenyl) sulfone, bis (3- Bis (hydroxyaryl) sulfones such as phenyl-4-hydroxyphenyl) sulfone, 4,4′-dihydroxybiphenyl, 4,4′-dihydroxy-2,2′-dimethylbiphenyl, 4,4′-dihydroxy-3, 3'-dimethylbiphenyl, 4 , 4'-dihydroxy-3, 3'-dicyclohexylbiphenyl, 3,3'-difluoro-4,4'-dihydroxybiphenyl and the like. These can use 1 type (s) or 2 or more types.

  Examples of aromatic dihydroxy compounds other than the above general formula (I) include dihydroxybenzenes, halogen and alkyl-substituted dihydroxybenzenes. For example, resorcin, 3-methyl resorcin, 3-ethyl resorcin, 3-propyl resorcin, 3-butyl resorcin, 3-t-butyl resorcin, 3-phenyl resorcin, 3-cumyl resorcin, 2,3,4,6- Tetrafluororesorcin, 2,3,4,6-tetrabromoresorcin, catechol, hydroquinone, 3-methylhydroquinone, 3-ethylhydroquinone, 3-propylhydroquinone, 3-butylhydroquinone, 3-t-butylhydroquinone, 3-phenyl Hydroquinone, 3-cumylhydroquinone, 2,5-dichlorohydroquinone, 2,3,5,6-tetramethylhydroquinone, 2,3,4,6-tetra-t-butylhydroquinone, 2,3,5,6- Tetrafluorohydroquinone, 2, 3, 5, - tetrabromo hydroquinone, and the like. These can use 1 type (s) or 2 or more types.

  Examples of the aliphatic dihydroxy compound include butane-1,4-diol, 2,2-dimethylpropane-1,3-diol, hexane-1,6-diol, diethylene glycol, triethylene glycol, tetraethylene glycol, and octaethylene. Glycol, dipropylene glycol, N, N-methyldiethanolamine, cyclohexane-1,3-diol, cyclohexane-1,4-diol, 1,4-dimethylolcyclohexane, p-xylylene glycol, 2,2-bis -(4-hydroxycyclohexyl) -propane and the like. These can use 1 type (s) or 2 or more types. Among these, bisphenol A which is an aromatic dihydroxy compound is preferable.

Furthermore, diesters of dihydroxy compounds, dicarbonates of dihydroxy compounds, monocarbonates of dihydroxy compounds, and the like can also be used. Examples of diesters of dihydroxy compounds include bisphenol A diacetate, bisphenol A dipropionate, bisphenol A dibutyrate, and bisphenol A dibenzoate. Examples of dicarbonates of dihydroxy compounds include bismethyl carbonate of bisphenol A, bisethyl carbonate of bisphenol A, and bisphenyl carbonate of bisphenol A. These can use 1 type (s) or 2 or more types.
Examples of monocarbonates of dihydroxy compounds include bisphenol A monomethyl carbonate, bisphenol A monoethyl carbonate, bisphenol A monopropyl carbonate, and bisphenol A monophenyl carbonate. These can use 1 type (s) or 2 or more types.

  Examples of the carbonic acid diester compound include diaryl carbonate compounds, dialkyl carbonate compounds, and alkylaryl carbonate compounds. The diaryl carbonate compound has the general formula (III)

（式中、Ａｒ^１及びＡｒ^２はそれぞれアリール基を示し、これらは互いに同一でも異なっていてもよい。）で表される化合物、又は一般式（ＩＶ）

(Wherein Ar ¹ and Ar ² each represent an aryl group, and these may be the same or different from each other), or a compound represented by the general formula (IV)

（式中、Ａｒ^３及びＡｒ^４はそれぞれアリール基を示し、これらは互いに同一でも異なっていてもよく、Ｄ^１は前記芳香族ジヒドロキシ化合物から水酸基２個を除いた残基を示す。）で表される化合物である。また、炭酸ジアルキル化合物は、一般式（Ｖ）

(Wherein Ar ³ and Ar ⁴ each represent an aryl group, which may be the same or different from each other, and D ¹ represents a residue obtained by removing two hydroxyl groups from the aromatic dihydroxy compound). It is a compound. The dialkyl carbonate compound is represented by the general formula (V)

（式中、Ｒ^５及びＲ^６はそれぞれ炭素数１〜６のアルキル基又は炭素数４〜７シクロアルキル基を示し、これらは互いに同一でも異なっていてもよい。）で表される化合物、又は一般式（ＶＩ）

(Wherein R ⁵ and R ⁶ each represent an alkyl group having 1 to 6 carbon atoms or a cycloalkyl group having 4 to 7 carbon atoms, which may be the same or different from each other), or Formula (VI)

（式中、Ｒ^７及びＲ^８はそれぞれ炭素数１〜６のアルキル基又は炭素数４〜７のシクロアルキル基を示し、これらは互いに同一でも異なっていてもよく、Ｄ^２は前記芳香族ジヒドロキシ化合物から水酸基２個を除いた残基を示す。）で表される化合物である。そして、炭酸アルキルアリール化合物は、一般式（ＶＩＩ）

(Wherein R ⁷ and R ⁸ each represent an alkyl group having 1 to 6 carbon atoms or a cycloalkyl group having 4 to 7 carbon atoms, which may be the same as or different from each other, and D ² represents the aromatic dihydroxy group. It shows a residue obtained by removing two hydroxyl groups from a compound.) The alkyl aryl carbonate compound is represented by the general formula (VII)

（式中、Ａｒ^５はアリール基、Ｒ^９は炭素数１〜６のアルキル基又は炭素数４〜７のシクロアルキル基を示す。）で表される化合物、又は一般式（ＶＩＩＩ）

(Wherein Ar ⁵ represents an aryl group, R ⁹ represents an alkyl group having 1 to 6 carbon atoms or a cycloalkyl group having 4 to 7 carbon atoms), or a general formula (VIII)

（式中、Ａｒ^６はアリール基、Ｒ^１０は炭素数１〜６のアルキル基又は炭素数４〜７のシクロアルキル基、Ｄ^３は前記芳香族ジヒドロキシ化合物から水酸基２個を除いた残基を示す。）で表される化合物である。

(In the formula, Ar ⁶ is an aryl group, R ¹⁰ is an alkyl group having 1 to 6 carbon atoms or a cycloalkyl group having 4 to 7 carbon atoms, and D ³ is a residue obtained by removing two hydroxyl groups from the aromatic dihydroxy compound. It is a compound represented by.

Here, examples of the diaryl carbonate compound include diphenyl carbonate, ditolyl carbonate, bis (chlorophenyl) carbonate, m-cresyl carbonate, dinaphthyl carbonate, bis (diphenyl) carbonate, bisphenol A bisphenyl carbonate, and the like. These can use 1 type (s) or 2 or more types.
Examples of the dialkyl carbonate compound include diethyl carbonate, dimethyl carbonate, dibutyl carbonate, dicyclohexyl carbonate, bisphenol A bismethyl carbonate, and the like. Examples of the alkyl aryl carbonate compound include methyl phenyl carbonate, ethyl phenyl carbonate, butyl phenyl carbonate, cyclohexyl phenyl carbonate, bisphenol A methyl phenyl carbonate, and the like. These can use 1 type (s) or 2 or more types. Of these, diphenyl carbonate is preferred.

  In producing such a polycarbonate, a molecular weight regulator, a catalyst and the like can be used as necessary. Examples of the molecular weight regulator include phenol, o- / m- / p-cresol, o- / m- / pn-butylphenol, o- / m- / p-isobutylphenol, o- / m- / p. -T-butylphenol, o- / m- / p-n-pentylphenol, o- / m- / p-hexylphenol, o- / m- / pn-octylphenol, o- / m- / pt -Octylphenol, o- / m- / p-cyclohexylphenol, o- / m- / p-phenylphenol, o- / m- / pn-nonylphenol, o- / m- / p-cumylphenol, o -/ M- / p-naphthylphenol, 2,6- / 2,5- / 2,4- / 3,5-di-t-butylphenol, 2,5- / 3,5-dicumylphenol, bromophenol , Tribromophenol Monoalkylphenol having a linear or branched alkyl group having an average carbon number of 12 to 35 in the ortho, meta or para position, 9- (4-hydroxyphenyl) -9- (4-methoxyphenyl) fluorene, 9 And monovalent phenols such as-(4-hydroxy-3-methylphenyl) -9- (4-methoxy-3-methylphenyl) fluorene and 4- (1-adamantyl) phenol. These can use 1 type (s) or 2 or more types.

  As the branching agent, a polyfunctional organic compound having three or more functional groups is used. Specifically, it has three or more functional groups such as hydroxyl group, carboxyl group, amino group, imino group, formyl group, acid halide group, haloformate group in one compound. For example, phloroglucin, merit acid, trimellit Acid, trimellitic chloride, trimellitic anhydride, gallic acid, n-propyl gallate, protocatechuic acid, pyromellitic acid, pyromellitic dianhydride, α-resorcinic acid, β-resorcinic acid, resorcinaldehyde, trime Lithyl chloride, trimethyltrichloride, 4-chloroformylphthalic anhydride, benzophenone tetracarboxylic acid, 2,4,4'-trihydroxybenzophenone, 2,2 ', 4,4'-tetrahydroxybenzophenone, 2,4, 4'-trihydroxyphenyl ether, 2,2 ', 4,4'-tetra Hydroxyphenyl ether, 2,4,4′-trihydroxydiphenyl-2-propane, 2,2′-bis (2,4-dihydroxy) propane, 2,2 ′, 4,4′-tetrahydroxydiphenylmethane, 2, 4,4′-trihydroxydiphenylmethane, 1- [α-methyl-α- (4′-hydroxyphenyl) ethyl] -4- [α ′, α′-bis (4 ″ -hydroxyphenyl) ethyl] benzene, α, α ′, α ″ -tris (4-hydroxyphenyl) -1,3,5-triisopropylbenzene, 2,6-bis (2′-hydroxy-5′-methylbenzyl) -4-methylphenol 4,6-dimethyl-2,4,6-tris (4′-hydroxyphenyl) -heptene-2, 4,6-dimethyl-2,4,6-dimethyl-tris (4-hydroxy Phenyl) -heptane-2,1,3,5-tris (4-hydroxyphenyl) -benzene, 1,1,1-tris (4′-hydroxyphenyl) -ethane, 2,2-bis [4,4- Bis (4′-hydroxyphenyl) cyclohexyl] -propane, 2,6-bis (2′-hydroxy-5′-isopropylbenzyl) -4-isopropylphenol, bis [2-hydroxy-3- (2′-hydroxy-) 5′-methylbenzyl) -5-methylphenyl] methane, bis [2-hydroxy-3- (2′-hydroxy-5′-isopropylbenzyl) -5-methylphenyl] methane, tetrakis (4-hydroxyphenyl) methane , Tris (4-hydroxyphenyl) phenylmethane, 2 ', 4,7-trihydroxyflavan, 2,4,4-trimethyl- 2 ′, 4′-dihydroxyphenylisopropyl) benzene, tris (4′-hydroxyaryl) -amyl-s-triazine, 1- [α-methyl-α- (4′-hydroxyphenyl) ethyl] -3- [α ', Α'-bis (4' '-hydroxyphenyl) ethyl] benzene, isatin bis (o-cresol), α, α, α', α'-tetrakis (4-hydroxyphenyl) -p-xylene, α, α , Α ′, α′-tetrakis (3-methyl-4-hydroxyphenyl) -p-xylene, α, α, α ′, α′-tetrakis (2-methyl-4-hydroxyphenyl) -p-xylene, α , Α, α ′, α′-tetrakis (2,5-dimethyl-4-hydroxyphenyl) -p-xylene, α, α, α ′, α′-tetrakis (2,6-dimethyl-4-hydroxyphenyl) p- xylene, alpha,. alpha .'- dimethyl -α, α, α ', α'- tetrakis (4-hydroxyphenyl)-p-xylene. These can use 1 type (s) or 2 or more types.

  The polycarbonate includes a block copolymer having a polycarbonate unit and a polymer unit other than the polycarbonate unit, in addition to a polymer composed only of the polycarbonate unit obtained by the above method. Examples of the polymer unit other than the polycarbonate include a polyether unit, a polyester unit, and a polyamide unit. Even when a general and easily available polycarbonate composed of only a polycarbonate unit is used as the polycarbonate, the physical properties and characteristics of the polyamide resin can be greatly modified.

  In the production method of polycarbonate, the interfacial polycondensation method using phosgene is reacted in the presence of an acid binder and an organic solvent. Examples of the acid binder include alkali metal hydroxides such as sodium hydroxide and potassium hydroxide, and amine compounds such as pyridine, and examples of the solvent include halogenated hydrocarbons such as methylene chloride and chlorobenzene. In order to accelerate the reaction, a catalyst such as a tertiary amine or a quaternary ammonium salt can also be used. The reaction temperature is usually 0 to 40 ° C., and the reaction time is several minutes to 5 hours.

  The melting method using the carbonic acid diester compound is carried out by a method in which a predetermined proportion of the dihydroxy compound and the carbonic acid diester compound are stirred while being heated under an inert gas atmosphere to distill the alcohol or phenols produced. The reaction temperature varies depending on the boiling point of the alcohol or phenol produced, but is usually in the range of 120 to 300 ° C. The reaction is completed while distilling off the alcohol or phenol produced by reducing the pressure from the beginning. Moreover, in order to accelerate | stimulate reaction, the catalyst for normal transesterification can also be used.

The molecular weight of the polycarbonate is not particularly limited, but the viscosity average molecular weight (Mv) is preferably 3,000 to 150,000, more preferably 5,000 to 100,000, and 10,000 to 50,000. More preferably, it is 000. The viscosity average molecular weight (Mv) was determined by measuring the specific viscosity (η _SP ) from a solution of 0.7 g of polycarbonate dissolved in 100 ml of methylene chloride at 20 ° C. to determine the intrinsic viscosity [η], and the formula [η] = 1. It is calculated by 23 × 10 ⁻⁴ × (Mv) ^0.83 . Specific viscosity (η _SP ) = (t−t ₀ ) / t _{0, where} t ₀ is the drop time of methylene chloride and t is the drop time of the sample solution], the intrinsic viscosity [η] and the relative viscosity (η _SP ) satisfies the relationship of the formula η _SP /c=[η]+0.45×[η] ² c (where [η] is the intrinsic viscosity). Where c is the polymer concentration in the methylene chloride solution.

  The compounding quantity of a polycarbonate is 0.5-5 mass parts with respect to a polyamide (A) and a polyamide (B) total 100 mass parts, and it is preferable that it is 0.75-3 mass parts, 1.0- More preferably, it is 2.5 parts by mass. When the blending amount of the polycarbonate is less than the above, the interlayer adhesive strength in the laminated tube is inferior, and when the above value is exceeded, strong foaming is observed during the production of the resin composition, chemical resistance, heat resistance, mechanical properties, etc. The characteristic properties of the polyamide (A) and the polyamide (B) are remarkably deteriorated.

  Furthermore, the polyamide (C) may be added to an antioxidant, a heat stabilizer, an ultraviolet absorber, a light stabilizer, a lubricant, an inorganic filler, an antistatic agent, a flame retardant, a crystallization accelerator, a plasticizer, if necessary. Agents, colorants, lubricants, impact resistance improvers, other thermoplastic resins, and the like may be added. In order to improve the low temperature impact resistance of the polyamide (C), it is preferable to add an impact resistance improving material, and the flexural modulus measured in accordance with ASTM D-790 described in the description of the polyamide (A). It is more preferable to add a polymer having a viscosity of 500 MPa or less.

  As a method for producing the polyamide (C), various known reaction methods such as a melt-kneading reaction method, a solution reaction method, a suspension dispersion reaction and the like can be used, but from an industrial viewpoint and ease of reaction operation. From the viewpoint, the melt kneading method is preferable. In the case of the melt-kneading method, polyamide (A), polyamide (B) and polycarbonate may be melt-kneaded after uniformly mixing other additives at a predetermined blending ratio as required. For mixing, a Henschel mixer, ribbon blender, V-type blender, etc. are used for uniform mixing, and for melt kneading, a Banbury mixer, kneader, roll, uniaxial or biaxial multi-screw kneading extruder, etc. are used. The The melt kneading temperature can be appropriately selected according to the type of polyamide resin to be used in consideration of the reaction rate and the selectivity of the reaction, but is preferably 170 ° C to 350 ° C, and preferably 200 ° C to 300 ° C. Is more preferable. Melt kneading may be performed under normal pressure, reduced pressure, or pressurized conditions, and the time is a kneading time in a normal twin-screw extruder, for example, about 20 seconds to 3 minutes. It is not limited.

  The laminated tube according to the present invention comprises at least three layers including (a) layer made of polyamide (A), (b) layer made of polyamide (B), and (c) layer made of polyamide (C). It is a laminated tube.

  A preferred embodiment of the laminated tube is that the (c) layer is disposed between the (a) layer and the (b) layer. Thereby, it becomes possible to obtain a laminated tube having excellent interlayer adhesive strength. Moreover, it is essential to include the (b) layer. If the (b) layer is not included, the chemical solution permeation preventive property of the laminated tube is lowered. A more preferable embodiment of the laminated tube is that (a) layer is arranged in the outermost layer and (b) layer is arranged in the innermost layer. (A) By arrange | positioning a layer in the outermost layer, it becomes possible to obtain the laminated tube excellent in chemical resistance and a softness | flexibility. Moreover, it becomes possible to obtain the laminated tube excellent in chemical resistance and chemical | medical solution permeation | transmission prevention property by arrange | positioning (b) layer in the innermost layer.

  Further, in the laminated tube of the present invention, when the layer made of the polyamide composition containing the polyamide (B) and the conductive filler is disposed in the innermost layer, it is excellent in chemical resistance and chemical permeation preventing property, and fuel piping tube As a result, it is possible to prevent the spark generated by the internal friction of the fuel circulating in the pipe or the friction with the pipe wall from igniting the fuel. At that time, a layer made of polyoxamide containing no conductive filler is disposed outside the layer containing the conductive filler, so that both low temperature impact resistance and conductivity can be achieved. It is also economically advantageous.

Conductivity means that, for example, when a flammable fluid such as gasoline is continuously in contact with an insulator such as resin, static electricity may accumulate and ignite, but this static electricity will not accumulate. Says having electrical properties. This makes it possible to prevent an explosion due to static electricity generated when a fluid such as fuel is conveyed.
The conductive filler includes all fillers added to impart conductive performance to the resin, and examples thereof include granular, flaky and fibrous fillers.

  Examples of the particulate filler include carbon black and graphite. Examples of the flaky filler include aluminum flakes, nickel flakes, and nickel-coated mica. Examples of the fibrous filler include carbon fibers, carbon-coated ceramic fibers, carbon whiskers, carbon nanotubes, aluminum fibers, copper fibers, brass fibers, and stainless steel fibers. These can use 1 type (s) or 2 or more types. Among these, carbon nanotubes and / or carbon black are preferable.

  Carbon nanotubes are what are called hollow carbon fibrils, which have an outer region consisting of an essentially continuous multi-layer of regularly arranged carbon atoms and an inner hollow region, each layer And the hollow region are essentially cylindrical fibrils arranged substantially concentrically around the cylindrical axis of the fibrils. Furthermore, the regularly arranged carbon atoms in the outer region are preferably graphite-like, and the diameter of the hollow region is preferably 2 to 20 nm. The outer diameter of the carbon nanotube is preferably 3.5 to 70 nm, and more preferably 4 to 60 nm. If the outer diameter is less than the above value, the dispersibility in the resin may be inferior. On the other hand, if the outer diameter exceeds the above value, the resulting resin molded article may have poor conductivity. The aspect ratio (referring to the ratio of length / outer diameter) of the carbon nanotube is preferably 5 or more, more preferably 100 or more, and further preferably 500 or more. By satisfying the aspect ratio, it is easy to form a conductive network, and excellent conductivity can be exhibited by addition of a small amount.

  Carbon black includes all carbon blacks that are commonly used to impart conductivity. Preferred carbon blacks include acetylene black obtained by incomplete combustion of acetylene gas, and furnace-type incompleteness using crude oil as a raw material. Examples include, but are not limited to, furnace black such as ketjen black produced by combustion, oil black, naphthalene black, thermal black, lamp black, channel black, roll black, and disk black. Among these, acetylene black and / or furnace black are more preferable.

Carbon black is produced in various carbon powders having different characteristics such as particle diameter, surface area, DBP oil absorption, ash content and the like. Although there is no restriction | limiting in the characteristic of this carbon black, What has a favorable chain structure and a large aggregation density is preferable. A large amount of carbon black is not preferable in terms of impact resistance, and from the viewpoint of obtaining excellent electrical conductivity with a smaller amount, the average particle size is preferably 500 nm or less, more preferably 5 to 100 nm, The surface area (BET method) is preferably 10 m ² / g or more, more preferably 30 m ² / g or more, and further preferably 50 m ² / g or more. Further, the DBP (dibutyl phthalate) oil absorption is preferably 50 ml / 100 g or more, more preferably 100 ml / 100 g, further preferably 150 ml / 100 g or more. The ash content is preferably 0.5% by mass or less, and more preferably 0.3% by mass or less. The DBP oil absorption here is a value measured by a method defined in ASTM D-2414. Further, the carbon black preferably has a volatile content of less than 1.0% by mass.
These conductive fillers may be surface-treated with a titanate-based, aluminum-based or silane-based surface treatment agent. It is also possible to use a granulated product to improve melt kneading workability.

Since the blending amount of the conductive filler varies depending on the type of the conductive filler to be used, it cannot be specified unconditionally, but from the viewpoint of balance between conductivity, fluidity, mechanical strength, etc., 100 parts by mass of polyamide (B) On the other hand, it is generally preferably 3 to 30 parts by mass.
In addition, from the viewpoint of obtaining sufficient antistatic performance, the conductive filler preferably has a surface specific resistance value of the melt-extruded product of 10 ⁸ Ω / square or less, particularly 10 ⁶ Ω / square or less. More preferred. However, the blending of the conductive filler tends to cause deterioration of strength and fluidity. Therefore, if the target conductivity level is obtained, it is desirable that the amount of the conductive filler is as small as possible.

[Laminated tube]
In the laminated tube of the present invention, the thickness of each layer is not particularly limited, and can be adjusted according to the type of polymer constituting each layer, the total number of layers in the laminated tube, usage, etc., but the thickness of each layer is The thickness of the (a) layer, (b) layer, and (c) layer is generally determined by considering the properties of the laminated tube such as alcohol gasoline permeation prevention, low temperature impact resistance, and flexibility. It is preferable that it is 3-90% with respect to the thickness of the whole tube, respectively. Considering the chemical solution permeation prevention property, the thickness of the layer (b) is more preferably 5 to 50%, and further preferably 7 to 30% with respect to the thickness of the entire laminated tube.

  The total number of layers in the laminated tube of the present invention is not particularly limited as long as it is at least three layers including the (a) layer, the (b) layer, and the (c) layer. Although the number of layers of the laminated tube of the present invention is 3 or more, it is preferably 8 or less, more preferably 3 to 7 layers as judged from the mechanism of the tube production apparatus.

As a preferable layer structure of the laminated tube of the present invention, (a) / (c) / (b), (a) / (c) / (b ′), (a) / (c) / (b) / (b '), (A) / (c) / (b) / (c) / (a), (a) / (c) / (b) / (c) / (b), (a) / (c) Examples include / (b) / (c) / (b ′), but are not limited thereto.
In addition to the three layers (a), (b), and (c), the laminated tube of the present invention has other functions in order to provide additional functions or to obtain an economically advantageous laminated tube. You may have the layer which consists of a thermoplastic resin 1 layer or 2 layers or more.

  As other thermoplastic resins, other than polyamide (A) and polyamide (B), polymetaxylylene adipamide (polyamide MXD6), polymetaxylylene veramide (polyamide MXD8), polymetaxylylene azelamide (polyamide MXD9) ), Polymetaxylylene sebacamide (polyamide MXD10), polymetaxylylene dodecamide (polyamide MXD12), polymetaxylylene terephthalamide (polyamide MXDT), polymetaxylylene isophthalamide (polyamide MXDI), polymetaxylylene naphthalamide (Polyamide MXDN), polybis (4-aminocyclohexyl) methane dodecamide (polyamide PACM12), polybis (4-aminocyclohexyl) methane terephthalamide (polyamide PACMT), polybi (4-aminocyclohexyl) methane isophthalamide (polyamide PACMI), polyisophorone adipamide (polyamide IPD6), polyisophorone terephthalamide (polyamide IPDT), polyhexamethylene terephthalamide (polyamide 6T), polyhexamethylene isophthalamide (Polyamide 6I), polytrimethylhexamethylene terephthalamide (polyamide TMHT), polynonamethylene terephthalamide (polyamide 9T), polynonamethylene isophthalamide (polyamide 9I), polynonamethylene naphthalamide (polyamide 9N), Polynonamethylene hexahydroterephthalamide (polyamide 9T (H)), polydecamethylene terephthalamide (polyamide 10T), polydecamethylene isophthalamide (polyamide 10I) , Polydecamethylene naphthalamide (polyamide 10N), polydecamethylene hexahydroterephthalamide (polyamide 10T (H)), polyundecamethylene terephthalamide (polyamide 11T), polyundecamethylene isophthalamide (polyamide 11I) ), Polyundecamethylene naphthalamide (polyamide 11N), polyundecamethylene hexahydroterephthalamide (polyamide 11T (H)), polydodecamethylene terephthalamide (polyamide 12T), polydodecamethylene isophthalamide (polyamide) 12I), polydodecamethylenenaphthalamide (polyamide 12N), polydodecamethylenehexahydroterephthalamide (polyamide 12T (H)), and polyamide resins such as copolymers using these polyamide raw materials monomers. It is.

  In addition, polybutylene terephthalate (PBT), polyethylene terephthalate (PET), polyethylene isophthalate (PEI), PET / PEI copolymer, polytrimethylene terephthalate (PTT), polyarylate (PAR), polyethylene naphthalate (PEN), Polyester resins such as polybutylene naphthalate (PBN), liquid crystal polyester (LCP), polylactic acid (PLA), polyglycolic acid (PGA), polyvinylidene fluoride (PVDF), polyvinyl fluoride (PVF), polytetrafluoroethylene (PTFE), polychlorotrifluoroethylene (PCTFE), tetrafluoroethylene / perfluoroalkyl vinyl ether copolymer (PFA), tetrafluoroethylene / hexafluoropropylene copolymer ( EP), tetrafluoroethylene / perfluoroalkyl vinyl ether / hexafluoropropylene copolymer, ethylene / tetrafluoroethylene copolymer (ETFE), ethylene / tetrafluoroethylene / hexafluoropropylene copolymer (EFEP), vinylidene fluoride / Tetrafluoroethylene copolymer, vinylidene fluoride / hexafluoropropylene copolymer, vinylidene fluoride / perfluoroalkyl vinyl ether copolymer, tetrafluoroethylene / hexafluoropropylene / vinylidene fluoride copolymer (THV), fluorine Vinylidene fluoride / perfluoroalkyl vinyl ether / tetrafluoroethylene copolymer, ethylene / chlorotrifluoroethylene copolymer (ECTFE), chlorotrifluoroethylene / teto Fluoroethylene copolymer, vinylidene fluoride / chlorotrifluoroethylene copolymer, chlorotrifluoroethylene / perfluoroalkyl vinyl ether copolymer, chlorotrifluoroethylene / hexafluoropropylene copolymer, chlorotrifluoroethylene / tetrafluoro Ethylene / hexafluoropropylene copolymer, chlorotrifluoroethylene / tetrafluoroethylene / vinylidene fluoride copolymer, chlorotrifluoroethylene / tetrafluoroethylene / perfluoroalkyl vinyl ether copolymer, chlorotrifluoroethylene / perfluoroalkyl Vinyl ether / hexafluoropropylene copolymer, chlorotrifluoroethylene / tetrafluoroethylene / hexafluoropropylene / perfluoroal Examples thereof include fluorine resins such as a kill vinyl ether copolymer and a chlorotrifluoroethylene / tetrafluoroethylene / vinylidene fluoride / perfluoroalkyl vinyl ether copolymer.

  Furthermore, high density polyethylene (HDPE), medium density polyethylene (MDPE), low density polyethylene (LDPE), linear low density polyethylene (LLDPE), ultra high molecular weight polyethylene (UHMWPE), polypropylene (PP), ethylene / propylene Polymer (EPR), ethylene / butene copolymer (EBR), ethylene / vinyl acetate copolymer (EVA), saponified ethylene / vinyl acetate copolymer (EVOH), ethylene / acrylic acid copolymer (EAA) Polyolefins such as ethylene / methacrylic acid copolymer (EMAA), ethylene / methyl acrylate copolymer (EMA), ethylene / methyl methacrylate copolymer (EMMA), ethylene / ethyl acrylate copolymer (EEA) Resin and acrylic acid, methacrylic acid, maleic acid, Malic acid, itaconic acid, crotonic acid, mesaconic acid, citraconic acid, glutaconic acid, cis-4-cyclohexene-1,2-dicarboxylic acid, endobicyclo- [2.2.1] -5-heptene-2,3- Carboxyl groups such as dicarboxylic acids and their metal salts (Na, Zn, K, Ca, Mg), maleic anhydride, itaconic anhydride, citraconic anhydride, endobicyclo- [2.2.1] -5-heptene-2 The above polyolefin resin containing functional groups such as epoxy groups such as acid anhydride groups such as 1,3-dicarboxylic acid anhydride, glycidyl acrylate, glycidyl methacrylate, glycidyl ethacrylate, glycidyl itaconate, glycidyl citraconic acid, etc. , Polyether resins such as polyacetal (POM) and polyphenylene oxide (PPO), polysulfone (P F), polysulfone resins such as polyethersulfone (PES), polyphenylene sulfide (PPS), polythioether resins such as polythioethersulfone (PTES), polyetheretherketone (PEEK), polyallyletherketone (PAEK) Such as polyketone resins, polyacrylonitrile (PAN), polymethacrylonitrile, acrylonitrile / styrene copolymer (AS), methacrylonitrile / styrene copolymer, acrylonitrile / butadiene / styrene copolymer (ABS), methacrylo Polynitrile resins such as nitrile / styrene / butadiene copolymer (MBS), polymethacrylate resins such as polymethyl methacrylate (PMMA) and polyethyl methacrylate (PEMA), polyvinyl acetate (PVAc), etc. Polyvinyl ester resins, polyvinylidene chloride (PVDC), polyvinyl chloride (PVC), polyvinyl chloride / vinylidene chloride copolymers, polyvinyl chloride resins such as vinylidene chloride / methyl acrylate copolymers, cellulose acetate, cellulose butyrate, etc. Cellulose resin, polycarbonate resin such as polycarbonate (PC), polyimide resin such as thermoplastic polyimide (PI), polyamideimide (PAI), polyetherimide, thermoplastic polyurethane resin, polyamide elastomer, polyurethane elastomer, etc. Can be mentioned.

  It is also possible to laminate any substrate other than thermoplastic resin, such as paper, metal-based material, non-stretched, uniaxially or biaxially stretched plastic film or sheet, woven fabric, non-woven fabric, metal cotton, wood, etc. is there. Examples of the metal-based material include aluminum, iron, copper, nickel, gold, silver, titanium, molybdenum, magnesium, manganese, lead, tin, chromium, beryllium, tungsten, cobalt, and other metals and metal compounds, and two or more of these. Examples include alloy steels such as stainless steel, aluminum alloys, copper alloys such as brass and bronze, and alloys such as nickel alloys.

  As a laminated tube manufacturing method, using an extruder corresponding to the number of layers or the number of materials, melt extrusion, a method of simultaneously laminating inside or outside the die (coextrusion method), or a single layer tube or There is a method (coating method) in which the laminated tube produced by the above method is produced in advance and laminated on the outside sequentially using an adhesive if necessary. The laminated tube of the present invention is preferably produced by coextrusion molding in which various materials are coextruded in a molten state, and various materials are heat-sealed (melt-bonded) to produce a laminated tube in one step.

  In addition, when the obtained laminated tube has a complicated shape, or when subjected to heat bending after molding to form a molded product, in order to remove the residual distortion of the molded product, after forming the above laminated tube, It is also possible to obtain a desired molded article by heat treatment for 0.01 to 10 hours at a temperature lower than the lowest melting point of the resin constituting the tube.

  The laminated tube may have a corrugated region. The waveform region is a region formed in a waveform shape, a bellows shape, an accordion shape, a corrugated shape, or the like. The corrugated region is not limited to having the entire length of the laminated tube, but may be partially provided in an appropriate region on the way. The corrugated region can be easily formed by first forming a straight tube and then molding it to obtain a predetermined corrugated shape or the like. By having such a corrugated region, it has shock absorption and attachment is easy. Furthermore, for example, necessary parts such as a connector can be added, or an L shape or a U shape can be formed by bending.

  In all or part of the outer periphery of the laminated tube thus formed, epichlorohydrin rubber (ECO), acrylonitrile / butadiene rubber (NBR), NBR, and poly, considering stone wear, wear with other parts, and flame resistance Mixture of vinyl chloride, chlorosulfonated polyethylene rubber, chlorinated polyethylene rubber, acrylic rubber (ACM), chloroprene rubber (CR), ethylene / propylene rubber (EPR), ethylene / propylene / diene rubber (EPDM), mixture of NBR and EPDM A solid or sponge-like protective member (protector) made of a thermoplastic elastomer such as rubber, vinyl chloride, olefin, ester or amide can be disposed. The protective member may be a sponge-like porous body by a known method. By using a porous body, a protective part that is lightweight and excellent in heat insulation can be formed. Moreover, material cost can also be reduced. Alternatively, the strength may be improved by adding glass fiber or the like. Although the shape of a protection member is not specifically limited, Usually, it is a block-shaped member which has a recessed part which receives a cylindrical member or a laminated tube. In the case of a cylindrical member, the laminated tube can be inserted later into a previously produced cylindrical member, or the cylindrical member can be coated and extruded onto the laminated tube to adhere both together. In order to bond the two, the adhesive is applied to the inner surface of the protective member or the concave surface as necessary, and the laminated tube is inserted or fitted into this, and the two are brought into close contact with each other, thereby integrating the laminated tube and the protective member. Forming a structure. It can also be reinforced with metal or the like.

  The outer diameter of the laminated tube takes into account the flow rate of fuel (eg gasoline), and the wall thickness is such that the fuel permeability does not increase, and the normal tube breaking pressure can be maintained. Although it is designed to have a thickness that can maintain flexibility with a satisfactory degree of ease of assembly work and vibration resistance during use, it is not limited. The outer diameter is preferably 4 to 300 mm, the inner diameter is 3 to 250 mm, and the wall thickness is preferably 0.5 to 25 mm.

  The laminated tube of the present invention includes machine parts such as automobile parts, internal combustion engines, electric tool housings, industrial materials, industrial materials, electrical / electronic parts, medical care, food, household / office supplies, building materials related parts, furniture. It can be used for various applications such as industrial parts.

  Moreover, since the laminated tube of the present invention is excellent in chemical solution permeation prevention properties, it is suitable for a chemical solution transport tube. Examples of the chemical solution include aromatic hydrocarbon solvents such as benzene, toluene, xylene, methanol, ethanol, propanol, butanol, pentanol, ethylene glycol, propylene glycol, diethylene glycol, phenol, cresol, polyethylene glycol, polypropylene glycol, and the like. Alcohol, phenol solvents, dimethyl ether, dipropyl ether, methyl-t-butyl ether, dioxane, tetrahydrofuran and other ether solvents, chloroform, methylene chloride, trichloroethylene, ethylene dichloride, perchlorethylene, monochloroethane, dichloroethane, tetrachloroethane Halogen solvents such as perchloroethane, chlorobenzene, acetone, methyl ethyl ketone, diethyl ketone, acetone Ketone solvents such as phenone, gasoline, kerosene, diesel gasoline, alcohol-containing gasoline, methyl-t-butyl ether, oxygen-containing gasoline, amine-containing gasoline, sour gasoline, castor oil base brake fluid, glycol ether brake fluid, borate ester Examples include brake fluid, brake fluid for extremely cold regions, silicone fluid brake fluid, mineral oil brake fluid, power steering oil, hydrogen sulfide oil, window washer fluid, engine coolant, urea solution, pharmaceutical agent, ink, paint, etc. . The laminated tube of the present invention is suitable as a tube for conveying the above chemical solution, specifically, a feed tube, a return tube, an evaporation tube, a fuel filler tube, an ORVR tube, a reserve tube, a fuel tube such as a vent tube, an oil Tube, oil drilling tube, brake tube, tube for window washer fluid, engine coolant (LLC) tube, reservoir tank tube, urea solution transport tube, cooler tube for cooling water, refrigerant, etc., air conditioner refrigerant tube, heater tube, Examples include load heating tubes, floor heating tubes, infrastructure supply tubes, fire extinguishers and fire extinguishing equipment tubes, medical cooling equipment tubes, ink, paint spray tubes, and other chemical solution tubes. In particular, it is suitable as a fuel tube.

Hereinafter, the present invention will be specifically described with reference to examples and comparative examples, but the present invention is not limited thereto.
In addition, the analysis and measurement of physical properties in Examples and Comparative Examples were performed as follows.

The properties of the polyamide resin were measured by the following method.
[Relative viscosity]
According to JIS K-6920, the measurement was performed in 96% sulfuric acid under the conditions of a polyamide concentration of 1% and a temperature of 25 ° C.

[Terminal carboxyl group concentration]
A predetermined amount of polyamide sample is placed in a three-neck pear-shaped flask, 40 mL of benzyl alcohol is added, and then immersed in an oil bath set at 180 ° C. under a nitrogen stream. The mixture was stirred and dissolved by a stirring motor attached to the upper part, and titrated with 0.05N sodium hydroxide solution using phenolphthalein as an indicator to determine the terminal carboxyl group concentration.

[Terminal amino group concentration]
Put a predetermined amount of polyamide sample in a conical flask with a stopcock, add 40 mL of a pre-adjusted solvent phenol / methanol (volume ratio 9/1), stir and dissolve with a magnetic stirrer, and use thymol blue as an indicator Then, titration with 0.05N hydrochloric acid was performed to determine the terminal amino group concentration.

Moreover, each physical property of the laminated tube was measured by the following method.
[Low temperature impact resistance]
The impact test was performed at -40 ° C by the method described in SAE J-2260 7.5.

[Permeability of chemical solution (alcohol-containing gasoline) permeation]
One end of a tube cut to 200 mm was sealed, and alcohol-containing gasoline (CE10) mixed in isooctane / toluene / ethanol = 45/45/10 vol%, isooctane / toluene / ethanol 7.5 / 7.5 / 85 Alcohol-containing gasoline (CE85) mixed with 100% by volume and ethanol 100% by volume (E100) were added, and the remaining ends were sealed. Thereafter, the entire mass was measured, and then the test tube was placed in an oven at 60 ° C., and the mass change was measured every day. The change in mass per day was divided by the surface area of the inner layer per 1 m of the tube to calculate the alcohol-containing gasoline permeation amount (g / m ² · day).

[Interlayer adhesion]
The tube cut to 200 mm was further cut in half in the vertical direction to create a test piece. Using a universal material testing machine (Tensilon UTM III-200, manufactured by Orientec Co., Ltd.), a 180 ° peel test was performed at a tensile speed of 50 mm / min. The peel strength was read from the maximum point of the SS curve, and the interlayer adhesion was evaluated.

[Durability of interlayer adhesion strength in high temperature atmosphere]
A sample obtained by cutting a laminated tube into a length of 20 cm was used as a sample. This sample was set in a constant temperature bath at 100 ° C. and held for 250 hours. Thereafter, the tube was taken out, the adhesive strength was measured by the above method, and the durability of the interlayer adhesive strength in a high temperature atmosphere was evaluated.

[Materials Used in Examples and Comparative Examples]
Polyamide (A)
(A-1) Manufacture of polyamide 12 A 70 liter autoclave was charged with 20 kg of dodecane lactam, 0.5 kg of water and 49.3 g of 5-amino-1,3,3-trimethylcyclohexanemethylamine, and the inside of the polymerization tank was replaced with nitrogen. Then, the mixture was heated to 180 ° C. and stirred at this temperature so that the inside of the reaction system became uniform. Subsequently, the temperature in the polymerization tank was raised to 270 ° C., and polymerization was performed with stirring for 2 hours while adjusting the pressure in the tank to 3.5 MPa. Thereafter, the pressure was released to normal pressure over about 2 hours, and then the pressure was reduced to 53 kPa, and polymerization was performed for 4 hours under reduced pressure. Next, nitrogen was introduced into the autoclave, and after returning to normal pressure, the strand was extracted from the lower nozzle of the reaction vessel and cut to obtain pellets. The pellets were dried under reduced pressure to obtain polyamide 12 having a relative viscosity of 2.26, a terminal amino group concentration of 45 μeq / g, and a terminal carboxyl group concentration of 24 μeq / g (hereinafter, this polyamide 12 is referred to as (a-1) methylene). Ratio of the number of groups to the number of amide groups: 11, saturated water absorption: 1.6%). The terminal amino group concentration [A] (μeq / g) and the terminal carboxyl group concentration [B] (μeq / g) of (a-1) satisfy [A]> [B] +5.

(A-1) Manufacture of polyamide 12 resin composition In (a-1), maleic anhydride-modified ethylene / propylene copolymer (manufactured by JSR Corporation, JSR T7712SP) is mixed in advance as an impact resistance improver. Benzenesulfonic acid butyramide was injected as a plasticizer with a metering pump from the middle of the cylinder of the biaxial melt kneader while supplying to the axial melt kneader (Nippon Steel Works, Model: TEX44). After melt-kneading at a temperature of 180 to 260 ° C. and extruding the molten resin into a strand shape, this is introduced into a water tank, cooled, cut, and vacuum dried to give polyamide 12 resin 85 mass%, impact resistance improving material 10 mass%. Then, a pellet of a polyamide 12 resin composition comprising 5% by mass of a plasticizer was obtained (hereinafter, this polyamide resin composition is referred to as (A-1)).

(A-2) Production of polyamide 12 In the production of (a-1), 49.3 g of 5-amino-1,3,3-trimethylcyclohexanemethylamine was converted to polyethyleneimine (manufactured by Nippon Shokubai Co., Ltd., Epomin SP-12). ) Polyamide 12 having a relative viscosity of 1.90, a terminal amino group concentration of 122 μeq / g, and a terminal carboxyl group concentration of 17 μeq / g was prepared in the same manner as in the production of (a-1) except that it was changed to 92.0 g. (Hereinafter, this polyamide 12 is referred to as (a-2). The ratio of the number of methylene groups to the number of amide groups: 11, saturated water absorption: 1.6%). The terminal amino group concentration [A] (μeq / g) and terminal carboxyl group concentration [B] (μeq / g) of (a-2) satisfy [A]> [B] +5.

Polyamide (B)
(B-1) Production of polyoxamide A stirrer, a thermometer, a torque meter, a pressure gauge, a raw material inlet directly connected to a diaphragm pump, a nitrogen gas inlet, a pressure outlet, a pressure regulator, and an internal volume equipped with a polymer outlet A 150 liter pressure vessel was charged with 28.40 kg (140.4 mol) of dibutyl oxalate, and the pressure inside the pressure vessel was pressurized to 0.5 MPa with 99.9999% nitrogen gas. The operation of releasing the gas was repeated 5 times, and after nitrogen substitution, the system was heated while stirring under a sealing pressure. After adjusting the temperature of dibutyl oxalate to 100 ° C. over about 30 minutes, 18.89 kg (119.3 mol) of 1,9-nonanediamine and 3.34 kg (21.1 mol) of 2-methyl-1,8-octanediamine (Mole ratio of 1,9-nonanediamine and 2-methyl-1,8-octanediamine is 85:15) is fed into the reaction vessel by a diaphragm pump at a flow rate of 1.49 liter / min for about 17 minutes. The temperature rose simultaneously. The internal pressure in the pressure vessel immediately after the supply increased to 0.35 MPa by butanol generated by the polycondensation reaction, and the temperature of the polycondensate increased to about 170 ° C. Thereafter, the temperature was raised to 235 ° C. over 1 hour. Meanwhile, the internal pressure was adjusted to 0.5 MPa while extracting the generated butanol from the pressure relief port. Immediately after the temperature of the polycondensate reached 235 ° C., butanol was extracted from the pressure release port over about 20 minutes, and the internal pressure was brought to normal pressure. The temperature was raised from normal pressure while flowing nitrogen gas at 1.5 liters / minute, and the temperature of the polycondensate was increased to 270 ° C. over about 1 hour and reacted at 270 ° C. for 4.5 hours. . Thereafter, stirring was stopped, the inside of the system was pressurized to 1 MPa with nitrogen and allowed to stand for about 10 minutes, then released to an internal pressure of 0.5 MPa, and the polycondensate was extracted in a string form from the lower outlet of the pressure vessel. The string-like polycondensate was immediately cooled, and the water-cooled string-like resin was pelletized by a pelletizer to obtain a polyoxamide having a melting point of 235 ° C. and a relative viscosity of 3.36 (hereinafter, this polyoxamide is referred to as (b-1)). .)

(B-1) Manufacture of polyoxamide resin composition (b-1) and maleic anhydride-modified ethylene / propylene copolymer (manufactured by JSR Corporation, JSR T7761P) as an impact resistance improver are mixed in advance and biaxially melted Supply to a kneading machine (Nippon Steel Works, Model: TEX44), melt knead at a cylinder temperature of 220-270 ° C., extrude the molten resin into a strand, introduce it into a water tank, cool, cut Then, vacuum drying was performed to obtain pellets of a polyoxamide resin composition comprising 85% by mass of (b-1) and 15% by mass of an impact resistance improving material (hereinafter, this polyoxamide resin composition is referred to as (B-1)). .

(B-2) Production of polyoxamide In production of (b-1), 1,89-nonanediamine 18.89 kg (119.3 mol) and 2-methyl-1,8-octanediamine 3.34 kg (21.1 mol) ) Is changed to 28.08 kg (140.4 mol) of 1,12-dodecanediamine, and the melting point is 235 ° C. and the relative viscosity is 3.02 in the same manner as in the production of (b-1). A polyoxamide was obtained (hereinafter, this polyoxamide is referred to as (b-2)).

(B-2) Production of polyoxamide resin composition Except that (b-1) was changed to (b-2) in the production of (B-1), the same method as in the production of (B-1), (B-2) A pellet of a polyoxamide resin composition comprising 85% by mass and 15% by mass of an impact resistance improving material was obtained (hereinafter, this polyoxamide resin composition is referred to as (B-2)).

(B-3) Production of polyoxamide In production of (b-1), 1,89-nonanediamine 18.89 kg (119.3 mol) and 2-methyl-1,8-octanediamine 3.34 kg (21.1 mol) ) Was changed to 24.15 kg (140.4 mol) of 1,10-dodecanediamine, and the melting point was 252 ° C. and the relative viscosity was 3.09 in the same manner as in the production of (b-1). A polyoxamide was obtained (hereinafter, this polyoxamide is referred to as (b-3)).

(B-3) Production of polyoxamide resin composition Except that (b-1) was changed to (b-3) in the production of (B-1), the same method as in the production of (B-1), (B-3) A pellet of a polyoxamide resin composition comprising 85% by mass and 15% by mass of an impact resistance improving material was obtained (hereinafter, this polyoxamide resin composition is referred to as (B-3)).

(B-4) Manufacture of polyoxamide The internal volume provided with the stirrer, the thermometer, the torque meter, the pressure gauge, the raw material inlet directly connected with the diaphragm pump, the nitrogen gas inlet, the pressure outlet, the pressure regulator, and the polymer outlet. A 150 liter pressure vessel was charged with 28.46 kg (140.7 moles) of dibutyl oxalate, pressurized to 0.5 MPa with 99.9999% nitrogen gas inside the pressure vessel, and then nitrogen up to atmospheric pressure. The operation of releasing the gas was repeated 5 times, and after nitrogen substitution, the system was heated while stirring under a sealing pressure. After the temperature of dibutyl oxalate was raised to 100 ° C. over about 30 minutes, 9.91 kg (62.6 mol) of 1,9-nonanediamine and 1.75 kg (11.0 mol) of 2-methyl-1,8-octanediamine And a mixture of 1.79 kg (67.0 mol) of 1,6-hexanediamine (molar ratio of 1,9-nonanediamine, 2-methyl-1,8-octanediamine and 1,6-hexanediamine is 44.5: 7.8: 47.7) was supplied into the reaction vessel over about 17 minutes at a flow rate of 1.49 liters / minute by means of a diaphragm pump, and the temperature was raised. The internal pressure in the pressure vessel immediately after the supply increased to 0.35 MPa by butanol generated by the polycondensation reaction, and the temperature of the polycondensate increased to about 170 ° C. Thereafter, the temperature was raised to 235 ° C. over 1 hour. Meanwhile, the internal pressure was adjusted to 0.75 MPa while extracting the generated butanol from the pressure relief port. Immediately after the temperature of the polycondensate reached 235 ° C., butanol was extracted from the pressure release port over about 20 minutes, and the internal pressure was brought to normal pressure. The temperature was raised from normal pressure while flowing nitrogen gas at 1.5 liters / minute, and the temperature of the polycondensate was increased to 270 ° C. over about 1 hour and reacted at 270 ° C. for 4.5 hours. . Thereafter, stirring was stopped and the system was pressurized to 1.0 MPa with nitrogen and allowed to stand for about 10 minutes, then released to an internal pressure of 0.5 MPa, and the polycondensate was extracted in a string form from the lower outlet of the pressure vessel. The string-like polycondensate was immediately cooled, and the water-cooled string-like resin was pelletized by a pelletizer to obtain a polyoxamide having a melting point of 251 ° C. and a relative viscosity of 3.26 (hereinafter, this polyoxamide is referred to as (b-4)). (The ratio of the number of methylene groups to the number of amide groups: 3.8, saturated water absorption: 1.3%).

(B-4) Production of polyoxamide resin composition Except that (b-1) was changed to (b-4) in the production of (B-1), the same method as in the production of (B-1), (B-4) A pellet of a polyoxamide resin composition comprising 85% by mass and 15% by mass of an impact resistance improving material was obtained (hereinafter, this polyoxamide resin composition is referred to as (B-4)).

(B-5) Production of conductive polyoxamide resin composition (In the production of B-2, maleic anhydride-modified ethylene / propylene copolymer (manufactured by JSR Corporation, JSR T7761P) was converted to maleic anhydride-modified ethylene / propylene copolymer. A method similar to the production of (B-2) except that the polymer (JSR Co., Ltd., JSR T7761P) and the conductive filler were changed to carbon black (Akzo Nobel Co., Ltd., Ketjen Black EC600JD). Thus, pellets of a conductive polyoxamide resin composition comprising (b-2) 79% by mass, impact resistance improving material 15% by mass, and conductive filler 6% by mass were obtained (hereinafter, this conductive polyoxamide resin composition ( B-5).).

Polyamide (C)
(C-1) Production of polyamide resin composition (a-1) includes (b-1), polycarbonate (Mitsubishi Engineering Plastics Co., Ltd., Iupilon S-3000, viscosity average molecular weight 21,000), improved impact resistance. A maleic anhydride-modified ethylene / propylene copolymer (manufactured by JSR Co., Ltd., JSR T7761P) is mixed in advance as a material and supplied to a twin-screw melt kneader (manufactured by Nippon Steel Co., Ltd., model: TEX44). After melt-kneading at a temperature of 200 to 280 ° C. and extruding the molten resin into a strand shape, this is introduced into a water tank, cooled, cut, and vacuum-dried to obtain (a-1) / (b-1) / polycarbonate / A pellet of a polyamide resin composition comprising an impact resistance improving material = 54/35/1/10 (mass ratio) was obtained (hereinafter, this polyamide resin composition is referred to as (C-1). Say.).

(C-2) Production of polyamide resin composition In the production of (C-1), except that (a-1) was changed to (a-2), the same method as in the production of (C-1) , (A-2) / (b-1) / polycarbonate / impact resistance improving material = 54/35/1/10 (mass ratio) to obtain a pellet of a polyamide resin composition (hereinafter, this polyamide resin composition) (Referred to as (C-2)).

(C-3) Production of polyamide resin composition In production of (C-1), except that (b-1) was changed to (b-2), the same method as in the production of (C-1) , (A-1) / (b-2) / polycarbonate / impact resistance improving material = 54/35/1/10 (mass ratio) to obtain a polyamide resin composition pellets (hereinafter, this polyamide resin composition) (Referred to as (C-3)).

(C-4) Production of polyamide resin composition In the production of (C-1), (b-1) was changed to (b-3) and the cylinder temperature was changed to 230 to 290 ° C (C-1 ) To obtain polyamide resin composition pellets of (a-1) / (b-3) / polycarbonate / impact resistance improving material = 54/35/1/10 (mass ratio). (Hereinafter, this polyamide resin composition is referred to as (C-4).)

(C-5) Production of polyamide resin composition In the production of (C-1), except that (b-1) was changed to (b-4), the same method as in the production of (C-1) , (A-1) / (b-4) / polycarbonate / impact resistance improving material = 54/35/1/10 (mass ratio) to obtain a polyamide resin composition pellets (hereinafter, this polyamide resin composition) (Referred to as (C-5)).

(C-6) Manufacture of polyamide resin composition In the manufacture of (C-1), except that the blending amount of the polycarbonate was changed, (a-1) / A pellet of a polyamide resin composition comprising (b-1) / polycarbonate / impact resistance improving material = 53/35/2/10 (mass ratio) was obtained (hereinafter, this polyamide resin composition is referred to as (C-6). .)

(C-7) Production of Polyamide Resin Composition (a-1) / (b-) in the production of (C-1), except that polycarbonate is not used, in the same manner as in the production of (C-1). 1) A pellet of a polyamide resin composition having an impact resistance improver = 55/35/10 (mass ratio) was obtained (hereinafter, this polyamide resin composition is referred to as (C-7)).

(C-8) Manufacture of polyamide resin composition In the manufacture of (C-1), except that the blending amount of polycarbonate was changed, (a-1) / (B-1) / Polycarbonate / Impact resistance improving material = 54.7 / 35 / 0.3 / 10 (mass ratio) to obtain a modified polyamide resin composition pellets (hereinafter referred to as this polyamide resin composition). (Referred to as C-8).

Adhesive resin (D)
(D-1) Maleic anhydride-modified polyethylene: Mitsui Chemicals, Admer NF528, MFR 2.2 g / 10 min (190 ° C., under 2160 g load), melting point 120 ° C.
(D-2) Ethylene / glycidyl methacrylate / vinyl acetate copolymer: manufactured by Sumitomo Chemical Co., Ltd., Bond First 2B, MFR 3.0 g / 10 min (under 190 ° C. and 2160 g load), melting point 95 ° C.
(D-3) Polyamide 6/12 copolymer: UBE Kosan Co., Ltd., UBE Nylon 7034U

Barrier resin (E)
(E-1) Saponified ethylene / vinyl acetate copolymer (EVOH): Nippon Synthetic Chemical Co., Ltd., Soarnol DC3203, ethylene content 32 mol%

Example 1
Using (A-1), (B-1) and (C-1) shown above, a (three-layer tube molding machine manufactured by Plastic Engineering Laboratory Co., Ltd.) (A-1) The extrusion temperature was 260 ° C., (B-1) was melted separately at an extrusion temperature of 270 ° C., and (C-1) was melted separately at an extrusion temperature of 270 ° C., and the discharged molten resin was merged with an adapter to form a laminated tubular body. . Subsequently, it is cooled by a sizing die for dimension control and taken up, and the (a) layer (outermost layer) composed of (A-1), the (b) layer (innermost layer) composed of (B-1), (C- (C) layer (intermediate layer) consisting of 1), the layer structure is (a) / (c) / (b) = 0.60 / 0.15 / 0.25 mm, the inner diameter is 6 mm, and the outer diameter is 8 mm. A laminated tube was obtained. The physical property measurement results of the laminated tube are shown in Table 1.

Example 2
A laminated tube having the layer structure shown in Table 1 was obtained in the same manner as in Example 1 except that (C-1) was changed to (C-2) in Example 1. The physical property measurement results of the laminated tube are shown in Table 1.

Example 3
In Example 1, except that (B-1) is changed to (B-2) and (C-1) is changed to (C-3), the layer configuration shown in Table 1 is the same as in Example 1. A laminated tube was obtained. The physical property measurement results of the laminated tube are shown in Table 1.

Example 4
In Example 1, (B-1) was changed to (B-3), (C-1) was changed to (C-4), and the extrusion temperature of (B-3) and (C-4) was 280 ° C. Except for the above, a laminated tube having the layer structure shown in Table 1 was obtained in the same manner as in Example 1. The physical property measurement results of the laminated tube are shown in Table 1.

Example 5
In Example 1, except that (B-1) is changed to (B-4) and (C-1) is changed to (C-5), the layer configuration shown in Table 1 is the same as in Example 1. A laminated tube was obtained. The physical property measurement results of the laminated tube are shown in Table 1.

Example 6
In Example 3, (B-2) was changed to (B-5), and the extrusion temperature of (B-5) was changed to 290 ° C., in the same manner as in Example 3, and the layers shown in Table 1 A laminated tube with a configuration was obtained. The physical property measurement results of the laminated tube are shown in Table 1. Moreover, when the electroconductivity of the said laminated tube was measured based on SAE J-2260, it was below 10 < ⁶ > ohm / square and it confirmed that it was excellent in the static electricity removal performance.

Example 7
A laminated tube having the layer structure shown in Table 1 was obtained in the same manner as in Example 1 except that (C-1) was changed to (C-6) in Example 1. The physical property measurement results of the laminated tube are shown in Table 1.

Example 8
Using (A-1), (B-2), (B-5), and (C-3), a 4-layer tube molding machine (manufactured by Plastic Engineering Laboratory Co., Ltd.) (A- 1) The extrusion temperature is 260 ° C., (B-2) and (B-5) are melted separately at an extrusion temperature of 290 ° C., and (C-3) is melted separately at an extrusion temperature of 270 ° C. Combined and formed into a laminated tubular body. Subsequently, it is cooled by a sizing die for dimension control and taken up, and (a) layer (outermost layer) composed of (A-1), (b) layer (inner layer) composed of (B-2), (B-5) ) (B ′) layer (innermost layer), (c) layer (intermediate layer) composed of (C-3), the layer structure is (a) / (c) / (b) / (b ′) = 0.60 / 0.15 / 0.15 / 0.10 mm, a laminated tube having an inner diameter of 6 mm and an outer diameter of 8 mm was obtained. The physical property measurement results of the laminated tube are shown in Table 1. Moreover, when the electroconductivity of the said laminated tube was measured based on SAE J-2260, it was below 10 < ⁶ > ohm / square and it confirmed that it was excellent in the static electricity removal performance.

Example 9
In Example 8, except that (B-2) was changed to (B-1) and (C-2) was changed to (C-1), the layer configuration shown in Table 1 was the same as in Example 8. A laminated tube was obtained. The physical property measurement results of the laminated tube are shown in Table 1. Moreover, when the electroconductivity of the said laminated tube was measured based on SAE J-2260, it was below 10 < ⁶ > ohm / square and it confirmed that it was excellent in the static electricity removal performance.

Comparative Example 1
In Example 1, the laminated tube of the layer structure shown in Table 1 was obtained by the method similar to Example 1 except not using (B-1) and (C-1). Table 1 shows the physical property measurement results of the single-layer tube.

Comparative Example 2
In Example 1, the tube of the layer structure shown in Table 1 was obtained by the same method as Example 1 except not using (C-1). Table 1 shows the physical property measurement results of the tube.

Comparative Example 3
A laminated tube having the layer structure shown in Table 1 was obtained in the same manner as in Example 1, except that (C-1) was changed to (C-7) in Example 1. The physical property measurement results of the laminated tube are shown in Table 1.

Comparative Example 4
A laminated tube having the layer structure shown in Table 1 was obtained in the same manner as in Example 1 except that (C-1) was changed to (C-8) in Example 1. The physical property measurement results of the laminated tube are shown in Table 1.

Comparative Example 5
In Example 1, except that (C-1) was changed to (D-1) maleic anhydride-modified polyethylene and the extrusion temperature of (D-1) was 200 ° C., the same method as in Example 1, A laminated tube having the layer structure shown in Table 1 was obtained. The physical property measurement results of the laminated tube are shown in Table 1.

Comparative Example 6
In Example 1, (C-1) was changed to (D-2) an ethylene / glycidyl methacrylate / vinyl acetate copolymer, and the extrusion temperature of (D-2) was changed to 180 ° C., as in Example 1. The laminated tube of the layer structure shown in Table 1 was obtained by this method. The physical property measurement results of the laminated tube are shown in Table 1.

Comparative Example 7
Upper (A-1), (D-3) Polyamide 6/12 copolymer, (E-1) Saponified ethylene / vinyl acetate copolymer Plabor (Plastics Engineering Laboratory Co., Ltd.) 5-layer tube molding In the machine, (A-1) is melted separately at an extrusion temperature of 250 ° C., (D-3) at an extrusion temperature of 220 ° C., and (E-1) is melted at an extrusion temperature of 230 ° C., and the discharged molten resin is an adapter. To form a laminated tubular body. Subsequently, it is cooled by a sizing die for dimension control and taken up, and (a) layer (outermost layer, innermost layer) made of (A-1), (D-3) made of polyamide 6/12 copolymer (d ) Layer (outer layer, inner layer), (E-1) layer configuration when (e) layer (intermediate layer) made of saponified ethylene / vinyl acetate copolymer is (a) / (d) / (e ) / (D) / (a) = 0.35 / 0.10 / 0.10 / 0.10 / 0.35 mm to obtain a laminated tube having an inner diameter of 6 mm and an outer diameter of 8 mm. The physical property measurement results of the laminated tube are shown in Table 1.

Claims (8)

A laminated tube consisting of at least three layers, including a (a) layer made of polyamide (A), a (b) layer made of polyamide (B), and a (c) layer made of polyamide (C),
The polyamide (A) is an aliphatic polyamide having a methylene group number / amide group number ratio of 5 or more and a methylene group number / amide group number of 5 or more and a saturated water absorption at 23 ° C. in water of 1.4% or more,
The polyamide (B) is a diamine unit containing 50 mol% or more of an aliphatic diamine unit having 9 to 13 carbon atoms based on all diamine units, and a dicarboxylic acid containing 60 mol% or more oxalic acid units based on all dicarboxylic acid units. A polyamide containing an oxamide bond unit comprising an acid unit;
A laminated tube in which the polyamide (C) is a polyamide resin composition containing 0.5 to 5 parts by mass of polycarbonate with respect to 100 parts by mass of the total of polyamide (A) and polyamide (B).   The laminated tube according to claim 1, wherein the (c) layer is disposed between the (a) layer and the (b) layer.   Polyamide (A) is polycaproamide (polyamide 6), polyhexamethylene adipamide (polyamide 66), polyhexamethylene sebamide (polyamide 610), polyhexamethylene dodecamide (polyamide 612), polydecamethylene At least selected from the group consisting of bacamide (polyamide 1010), polydecane methylene dodecane (polyamide 1012), poly dodecane methylene dodecane (polyamide 1212), polyundecanamide (polyamide 11), and polydodecanamide (polyamide 12). It is 1 type, The laminated tube of Claim 1 or 2 characterized by the above-mentioned.   The terminal amino group concentration [A] (μeq / g) and the terminal carboxyl group concentration [B] (μeq / g) of the polyamide (A) satisfy [A]> [B] +5. The laminated tube according to any one of 1 to 3.   5. The laminated tube according to claim 1, wherein (a) layer is disposed on the outermost layer and (b) layer is disposed on the innermost layer.   The laminated tube according to any one of claims 1 to 5, wherein a layer made of a polyamide composition containing polyamide (B) and a conductive filler is disposed in the innermost layer.   The laminated tube according to any one of claims 1 to 6, wherein the laminated tube is manufactured by coextrusion molding.   It is used as a fuel tube, The laminated tube of any one of Claim 1 to 7 characterized by the above-mentioned.