Fuel-contacting laminate

Abstract

To provide a laminate which exhibits excellent fuel low permeability to fuel containing a compound that is composed of only a carbon atom, a hydrogen atom and an oxygen atom, and has a carbonyl group or an ether bond.SOLUTION: There is provided a laminate contacting fuel, wherein the fuel contains at least a compound (1) which is composed of only a carbon atom, a hydrogen atom and an oxygen atom, and has a carbonyl group or an ether bond, and the laminate includes at least a non-fluorinated polymer layer containing at least one kind of non-fluorinated polymer selected from a group consisting of an ethylene-vinyl alcohol copolymer and aromatic polyamide.SELECTED DRAWING: None

Description

[Technical Field]

[0001] The present disclosure relates to laminates that come into contact with fuel. [Background technology]

[0002] Patent Document 1 describes a laminate structure composed of two or more layers, including at least (A) layer (a) made of an aliphatic polyamide, and (B) layer (b) made of a semi-aromatic polyamide composed of diamine units containing 60 mol % or more of aliphatic diamine units having 9 to 13 carbon atoms based on all diamine units, and dicarboxylic acid units containing 50 mol % or more of terephthalic acid and / or naphthalenedicarboxylic acid units based on all dicarboxylic acid units, and wherein layer (b) is disposed as the innermost layer. [Prior art documents] [Patent documents]

[0003] [Patent Document 1] International Publication No. 2005 / 102694 Summary of the Invention [Problem to be solved by the invention]

[0004] An object of the present disclosure is to provide a laminate that exhibits excellent low fuel permeability to a fuel that is composed only of carbon atoms, hydrogen atoms, and oxygen atoms and contains a compound having a carbonyl group or an ether bond. [Means for solving the problem]

[0005] According to the present disclosure, there is provided a laminate to be brought into contact with fuel, wherein the fuel contains at least a compound (1) consisting only of carbon atoms, hydrogen atoms, and oxygen atoms and having a carbonyl group or an ether bond, and the laminate includes at least a non-fluorinated polymer layer containing at least one non-fluorinated polymer selected from the group consisting of an ethylene / vinyl alcohol copolymer and an aromatic polyamide. [Effects of the Invention]

[0006] According to the present disclosure, it is possible to provide a laminate that exhibits excellent low fuel permeability to a fuel that is composed only of carbon atoms, hydrogen atoms, and oxygen atoms and contains a compound having a carbonyl group or an ether bond. DETAILED DESCRIPTION OF THE INVENTION

[0007] Specific embodiments of the present disclosure will be described in detail below, but the present disclosure is not limited to the following embodiments.

[0008] BACKGROUND ART Conventionally, laminates that exhibit low fuel permeability to gasoline or low fuel permeability to alcohol-containing gasoline have been known.

[0009] For example, Patent Document 1 describes that the fuel permeability coefficient of a laminated structure having the above-mentioned configuration was measured for alcohol-containing gasoline, which was a mixture of Fuel C (iso-octane / toluene = 50 / 50 volume ratio) and ethanol in a 90 / 10 volume ratio.

[0010] However, there has been no sufficient research to date into what kind of laminate structure is required to suppress the permeation of fuels that contain compounds that consist only of carbon atoms, hydrogen atoms, and oxygen atoms and have a carbonyl group or an ether bond.

[0011] It has now been found that by incorporating into a laminate a non-fluorinated polymer layer containing at least one non-fluorinated polymer selected from the group consisting of ethylene / vinyl alcohol copolymers and aromatic polyamides, the laminate exhibits surprisingly low fuel permeability to fuels containing compounds consisting only of carbon, hydrogen and oxygen atoms and having a carbonyl group or an ether bond.

[0012] That is, the laminate of the present disclosure is a laminate that comes into contact with fuel and contains at least a compound (1) consisting only of carbon atoms, hydrogen atoms, and oxygen atoms and having a carbonyl group or an ether bond, and includes at least a non-fluorinated polymer layer containing at least one non-fluorinated polymer selected from the group consisting of an ethylene / vinyl alcohol copolymer and an aromatic polyamide.

[0013] The configuration of the laminate of the present disclosure will be described in detail below.

[0014] (fuel) The laminate of the present disclosure is used in contact with a fuel that consists only of carbon, hydrogen, and oxygen atoms and contains at least a compound (1) having a carbonyl group or an ether bond. In one embodiment, the laminate of the present disclosure is used to inhibit permeation of a fuel that consists only of carbon, hydrogen, and oxygen atoms and contains at least a compound (1) having a carbonyl group or an ether bond. In one embodiment, the laminate of the present disclosure is a tube or hose that is used to distribute and / or inhibit permeation of a fuel that consists only of carbon, hydrogen, and oxygen atoms and contains at least a compound (1) having a carbonyl group or an ether bond. That is, the present disclosure includes the use of a laminate (tube or hose) for passing a fuel containing at least a compound (1) consisting only of carbon, hydrogen, and oxygen atoms and having a carbonyl group or an ether bond, and / or for suppressing the permeation of the fuel. The present disclosure also includes a method for distributing a fuel containing at least a compound (1) consisting only of carbon, hydrogen, and oxygen atoms and having a carbonyl group or an ether bond, the method comprising using a laminate (tube or hose) in contact with the fuel.

[0015] Compound (1) may be a compound synthesized from hydrogen and carbon dioxide. Compounds synthesized from hydrogen and carbon dioxide are also called synthetic fuels and are expected to contribute to reducing carbon dioxide emissions. The inventors' studies have revealed that while conventional laminates can inhibit the permeation of conventional fuels such as gasoline, diesel fuel, and alcohol fuel, they cannot sufficiently inhibit the permeation of such synthetic fuels. In other words, compound (1) exhibits permeability different from that of conventional fuels such as gasoline, diesel fuel, and alcohol fuel. Therefore, conventional knowledge cannot be utilized when selecting the layer configuration of a laminate to be used in contact with a fuel containing compound (1). Therefore, as a result of extensive studies, the inventors have discovered a laminate that exhibits low fuel permeability even for compound (1).

[0016] Compound (1) is preferably at least one selected from the group consisting of carbonate esters, chain ethers, and cyclic ethers, more preferably at least one selected from the group consisting of carbonate esters and cyclic ethers, and even more preferably carbonate esters.

[0017] Examples of compound (1) include dimethyl carbonate, diethyl carbonate, dimethyl ether, methyl tert-butyl ether (MTBE), oxymethylene dimethyl ether, and 1,3-dioxolane. The fuel contains one or more of these compounds. Of these, at least one compound selected from the group consisting of dimethyl carbonate and diethyl carbonate is preferred as compound (1).

[0018] The fuel may contain only the compound (1), or may contain the compound (1) and other fuels.

[0019] The fuel is, for example, A fuel containing only compound (1), a fuel containing compound (1) and an alcohol; a fuel containing compound (1) and gasoline; a fuel containing compound (1), alcohol, and gasoline; A fuel containing compound (1) and diesel fuel (light oil), Examples include:

[0020] The content of compound (1) in the fuel may be 0.1 to 100% by volume. The content of compound (1) in the fuel may be 1% by volume or more, 5% by volume or more, or 10% by volume or more. The content of compound (1) in the fuel may be 90% by volume or less, 80% by volume or less, 60% by volume or less, 40% by volume or less, or 20% by volume or less.

[0021] In one embodiment, the fuel contains compound (1) and an alcohol. The laminate of the present disclosure also exhibits excellent low permeability to fuels containing compound (1) and an alcohol.

[0022] The alcohol is preferably an alcohol having 1 to 5 carbon atoms, more preferably at least one selected from the group consisting of methanol, ethanol, propanol and butanol, and even more preferably at least one selected from the group consisting of methanol and ethanol.

[0023] The alcohol content in the fuel may be 10 to 99.9% by volume. The alcohol content in the fuel may be 20% by volume or more, 40% by volume or more, or 80% by volume or more. The alcohol content in the fuel may be 99% by volume or less, 95% by volume or less, or 90% by volume or less.

[0024] When the alcohol in the fuel is methanol, its content may be 10 to 99.9% by volume, and the content of methanol in the fuel may be 80% by volume or less, 50% by volume or less, 30% by volume or less, or 20% by volume or less.

[0025] In one embodiment, the fuel contains compound (1) and gasoline. The laminate of the present disclosure also exhibits excellent low permeability to fuel containing compound (1) and gasoline.

[0026] The gasoline may be obtained by refining crude oil. The boiling point of gasoline is generally 30 to 220°C.

[0027] The gasoline content in the fuel may be 10 to 99.9% by volume. The gasoline content in the fuel may be 20% by volume or more, 40% by volume or more, or 80% by volume or more. The gasoline content in the fuel may be 99% by volume or less, 95% by volume or less, or 90% by volume or less.

[0028] In one embodiment, the fuel does not include diesel fuel (gas oil). Diesel fuel may be obtained by refining crude oil. Diesel fuel generally has a boiling point greater than 220°C and less than or equal to 350°C.

[0029] In one embodiment, the fuel comprises compound (1) and diesel fuel (light oil).

[0030] Conventionally, aliphatic polyamides have been used as materials for forming tubes or hoses for diesel fuel, due to their excellent acid resistance, alkali resistance, hydrolysis resistance, physical properties, etc. Unlike gasoline or alcohol-containing fuels, diesel fuel (light oil) does not easily permeate aliphatic polyamide tubes, and therefore no consideration has been given to selecting materials from the perspective of suppressing diesel fuel permeation.

[0031] Compound (1) may be a compound synthesized from hydrogen and carbon dioxide. Compounds synthesized from hydrogen and carbon dioxide are also called synthetic fuels, and are expected to contribute to reducing carbon dioxide emissions. Diesel fuel (light oil), unlike gasoline and alcohol-containing fuels, is less likely to permeate aliphatic polyamide tubes. However, it has been found that when such synthetic fuels are blended with diesel fuel, the fuel permeates the tube and diffuses to the outside. Therefore, as a result of intensive research by the present inventors, a laminate exhibiting low fuel permeability to both diesel fuel and fuels containing compound (1) has been found.

[0032] That is, it has now been found that by introducing into a laminate a non-fluorinated polymer layer containing at least one non-fluorinated polymer selected from the group consisting of ethylene / vinyl alcohol copolymer and aromatic polyamide, the laminate exhibits surprisingly low fuel permeability to diesel fuel and fuels containing compounds consisting only of carbon, hydrogen and oxygen atoms and having a carbonyl group or an ether bond.

[0033] Diesel fuel may be obtained by refining crude oil and generally has a boiling point above 220°C and up to 350°C.

[0034] The content of diesel fuel in the fuel may be 10 to 99.9% by volume. The content of diesel fuel in the fuel may be 20% by volume or more, 40% by volume or more, or 80% by volume or more. The content of diesel fuel in the fuel may be 99% by volume or less, 95% by volume or less, or 90% by volume or less.

[0035] In one embodiment, the fuel does not include gasoline. Gasoline may be obtained by refining crude oil. The boiling point of gasoline is generally 30 to 220°C.

[0036] In one embodiment, the fuel does not contain alcohol, and examples of alcohol include alcohols having 1 to 5 carbon atoms.

[0037] (Non-fluorinated polymer layer (A)) The laminate of the present disclosure includes at least a non-fluorinated polymer layer (A) containing at least one non-fluorinated polymer (A) selected from the group consisting of ethylene / vinyl alcohol copolymers and aromatic polyamides.

[0038] As described above, the laminate of the present disclosure includes at least the non-fluorinated polymer layer (A), which contains at least one non-fluorinated polymer (A) selected from the group consisting of ethylene / vinyl alcohol copolymers and aromatic polyamides, and therefore exhibits excellent low fuel permeability to fuels containing compounds consisting only of carbon, hydrogen, and oxygen atoms and having a carbonyl group or an ether bond. Surprisingly, when a non-fluorinated polymer other than ethylene / vinyl alcohol copolymers and aromatic polyamides, for example, an aliphatic polyamide such as PA12, is used, sufficient low fuel permeability cannot be obtained.

[0039] The ethylene / vinyl alcohol copolymer used in the laminate of the present disclosure may be a thermoplastic resin. The ethylene / vinyl alcohol copolymer is obtained by saponifying an ethylene / vinyl acetate copolymer obtained from ethylene and vinyl acetate. The blending ratio of ethylene and vinyl acetate to be copolymerized is appropriately determined depending on the ratio of the moles of vinyl acetate units defined by the formula described below.

[0040] The ethylene / vinyl alcohol copolymer preferably has a vinyl acetate unit content of X mole % and a degree of saponification of Y mole % satisfying X×Y / 100≧7. If X×Y / 100<7, the interlayer adhesion may be insufficient. X×Y / 100≧10 is more preferable. The value of X×Y / 100 is an index of the hydroxyl group content of the ethylene / vinyl alcohol copolymer, and a large value of X×Y / 100 indicates a high hydroxyl group content of the ethylene / vinyl alcohol copolymer.

[0041] The hydroxyl group is a group that can be involved in adhesion between the EVOH layer and the mating material to be laminated, and a high content of hydroxyl groups in the ethylene / vinyl alcohol copolymer improves the interlayer adhesion in the laminate. In this disclosure, the above-mentioned "mating material to be laminated" refers to a material that is in contact with the mating material to be laminated.

[0042] In the present disclosure, the term "X mol% of vinyl acetate units" refers to the ratio of the number of moles [Ni] of vinyl acetate derived from vinyl acetate units to the total number of moles [N] of ethylene and vinyl acetate added in the molecule of an ethylene / vinyl alcohol copolymer, and is expressed by the following formula: Xi(%)=(Ni / N)×100 The vinyl acetate unit content X mole % is a value obtained by measurement using infrared absorption spectroscopy (IR).

[0043] In the present disclosure, the term "vinyl acetate unit" refers to a portion of the molecular structure of an ethylene / vinyl alcohol copolymer that is derived from vinyl acetate. The vinyl acetate unit may be saponified and have a hydroxyl group, or may be unsaponified and have an acetoxyl group.

[0044] The "saponification degree" is a percentage that represents the ratio of the number of saponified vinyl acetate units to the total number of saponified and unsaponified vinyl acetate units. The saponification degree is a value obtained by measurement using infrared absorption spectroscopy (IR).

[0045] Examples of ethylene / vinyl alcohol copolymers in which X and Y satisfy the above formula include commercially available products such as EVAL F101 (manufactured by Kuraray Co., Ltd., vinyl acetate unit X=68.0 mol %; degree of saponification Y=95%; X×Y / 100=64.6), MERSEN H6051 (manufactured by Tosoh Corporation, vinyl acetate unit X=11.2 mol %; degree of saponification Y=100%; X×Y / 100=11.2), and Technolink K200 (manufactured by Taoka Chemical Co., Ltd., vinyl acetate unit X=11.2 mol %; degree of saponification Y=85%; X×Y / 100=9.52).

[0046] The ethylene / vinyl alcohol copolymer preferably has an MFR of 0.5 g / 10 min or more at 200 ° C., and preferably 100 g / 10 min or less. MFRs of less than 0.5 g / 10 min or more than 100 g / 10 min tend to increase the difference between the melt viscosity of the ethylene / vinyl alcohol copolymer and that of the mating material, which is undesirable because it may cause uneven thickness of each layer. The preferred lower limit is 1 g / 10 min, and the preferred upper limit is 50 g / 10 min.

[0047] The aromatic polyamide used in the laminate of the present disclosure may be a thermoplastic resin. In the present disclosure, the aromatic polyamide includes semi-aromatic polyamides and fully aromatic polyamides. In one embodiment, the aromatic polyamide is a semi-aromatic polyamide containing aliphatic diamine units and aromatic dicarboxylic acid units.

[0048] Examples of aliphatic diamines 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, 1,11-undecanediamine, and 1,12-dodecanediamine. Of these, 1,6-hexanediamine and 1,9-nonanediamine are preferred.

[0049] Examples of aromatic dicarboxylic acids include terephthalic acid, phthalic acid, isophthalic acid, and naphthalenedicarboxylic acid, and among these, terephthalic acid is preferred.

[0050] The melting point of the semi-aromatic polyamide is preferably 200°C or higher, more preferably 250°C or higher, and preferably 350°C or lower.

[0051] Of the aromatic polyamides, polyamide 6T and polyamide 9T are preferred, and polyamide 9T is more preferred.

[0052] The non-fluorinated polymer layer (A) may contain various additives, such as stabilizers such as heat stabilizers, reinforcing agents, fillers, UV absorbers, pigments, etc., within the scope of the present disclosure. The use of such additives can improve the properties of the non-fluorinated polymer, such as thermal stability, surface hardness, abrasion resistance, antistatic properties, and weather resistance.

[0053] In one embodiment, the non-fluorinated polymer layer (A) is not electrically conductive. In one embodiment, the non-fluorinated polymer layer (A) does not contain a conductive filler.

[0054] (Conductive layer (N1)) The laminate of the present disclosure may further comprise a conductive layer (N1) that is conductive and contains a non-fluorinated polymer (N1). By providing the conductive layer (N1), it is possible to prevent the laminate from becoming charged even if static electricity is generated due to friction between the laminate and fuel.

[0055] Non-fluorinated polymers (N1) are polymers that do not contain fluorine atoms. A wide range of polymers known as thermoplastic resins can be used as non-fluorinated polymers (N1). Examples of non-fluorinated polymers (N1) include polyamide resins, polyolefin resins, vinyl chloride resins, polyurethane resins, polyester resins, polyaramid resins, polyimide resins, polyamide-imide resins, polyphenylene oxide resins, polyacetal resins, polycarbonate resins, acrylic resins, styrene resins, acrylonitrile / butadiene / styrene resins (ABS), cellulose resins, polyether ether ketone resins (PEEK), polysulfone resins, polyether sulfone resins (PES), polyetherimide resins, ethylene / vinyl alcohol copolymer resins, polyphenylene sulfide resins, polybutylene naphthalate resins, polybutylene terephthalate resins, and polyphthalamide (PPA).

[0056] The melting point of the non-fluorinated polymer (N1) is preferably 50°C or higher, more preferably 100°C or higher, even more preferably 150°C or higher, still more preferably 200°C or higher, particularly preferably 250°C or higher, and preferably 400°C or lower, more preferably 350°C or lower, still more preferably 300°C or lower, still more preferably 250°C or lower.

[0057] As the non-fluorinated polymer (N1) constituting the conductive layer (N1), aromatic polyamide is particularly preferred. As the aromatic polyamide, the same aromatic polyamide as that constituting the non-fluorinated polymer layer (A) can be used, and the same aromatic polyamide is preferred.

[0058] In one embodiment, the aromatic polyamide constituting the conductive layer (N1) is an aromatic polyamide containing an aliphatic diamine unit and an aromatic dicarboxylic acid unit.

[0059] As the aromatic polyamide constituting the conductive layer (N1), polyamide 6T and polyamide 9T are preferred, and polyamide 9T is more preferred.

[0060] The conductive layer (N1) preferably contains a conductive filler, which easily imparts conductivity to the conductive layer (N1), and further prevents the laminate from being charged even when static electricity is generated by friction between the laminate and fuel.

[0061] The conductive filler is not particularly limited, and examples thereof include conductive element powders or conductive element fibers of metals, carbon, etc.; powders of conductive compounds such as zinc oxide; and powders that have been surface-treated to be conductive.

[0062] The conductive elemental powder or conductive elemental fiber is not particularly limited, and examples thereof include metal powders such as copper and nickel; metal fibers such as iron and stainless steel; carbon black, carbon fibers, carbon fibrils, carbon nanotubes, and carbon nanohorns as described in JP-A-3-174018, etc.

[0063] The surface-conductively treated powder is a powder obtained by subjecting the surface of a non-conductive powder such as glass beads or titanium oxide to a conductive treatment. The method for the conductive treatment is not particularly limited, and examples thereof include metal sputtering and electroless plating. Among the conductive fillers described above, carbon black is preferably used because it is advantageous from the viewpoint of economy.

[0064] The amount of the conductive filler to be added is determined appropriately based on the type of non-fluorinated polymer (N1), the conductive performance required of the laminate, molding conditions, etc., but is preferably 1 part by mass or more and 30 parts by mass or less per 100 parts by mass of the non-fluorinated polymer (N1). A more preferred lower limit is 5 parts by mass, and a more preferred upper limit is 20 parts by mass.

[0065] In addition to the conductive filler, the conductive layer (N1) may contain various additives such as reinforcing agents, bulking agents, UV absorbers, pigments, etc., within the scope of the present disclosure. By using such additives, the properties of the conductive layer (N1), such as surface hardness, abrasion resistance, anti-static properties, and weather resistance, can be improved.

[0066] When the laminate of the present disclosure includes a conductive layer (N1), the conductive layer (N1) is preferably configured to come into contact with the fuel. By forming the contact surface between the laminate and the fuel with the conductive layer (N1), charging of the laminate can be further prevented even if static electricity is generated by friction between the laminate and the fuel.

[0067] (Fluororesin layer (F)) The laminate of the present disclosure may further include a fluororesin layer (F) containing a fluororesin. The fluororesin is a partially crystalline fluoropolymer, and is a fluoroplastic, not a fluororubber. The fluororesin has a melting point and exhibits thermoplasticity. The fluororesin may be melt-processable or non-melt-processable, but is preferably a melt-processable fluororesin because it allows for the production of a tube with high productivity by melt extrusion molding.

[0068] In this disclosure, melt-processable means that the polymer can be melted and processed using conventional processing equipment such as extruders, injection molding machines, etc. Thus, melt-processable fluororesins typically have a melt flow rate of 0.01 g / 10 min or more and 500 g / 10 min or less.

[0069] Examples of melt-processable fluororesins include tetrafluoroethylene (TFE) / perfluoro(alkyl vinyl ether) (PAVE) copolymers, tetrafluoroethylene (TFE) / hexafluoropropylene (HFP) copolymers, TFE / ethylene copolymers [ETFE], TFE / ethylene / HFP copolymers, polymers containing chlorotrifluoroethylene (CTFE) units, polyvinylidene fluoride [PVdF], TFE / vinylidene fluoride (VdF) copolymers [VT], polyvinyl fluoride [PVF], and TFE / HFP / VdF copolymers.

[0070] Examples of PAVE include perfluoro(methyl vinyl ether) (PMVE), perfluoro(ethyl vinyl ether) (PEVE), and perfluoro(propyl vinyl ether) (PPVE). Of these, PPVE is preferred. These may be used alone or in combination of two or more.

[0071] The fluororesin may contain polymerization units based on other monomers in an amount that does not impair the essential properties of each fluororesin. The other monomers can be appropriately selected from, for example, TFE, HFP, ethylene, propylene, perfluoro(alkyl vinyl ether), perfluoroalkylethylene, hydrofluoroolefin, fluoroalkylethylene, perfluoro(alkyl allyl ether), etc.

[0072] The melting point of the fluororesin is preferably 160°C or higher, more preferably 190°C or higher, even more preferably 230°C or higher, particularly preferably 240°C or higher, and preferably lower than 324°C, more preferably 320°C or lower, even more preferably 300°C or lower, particularly preferably 280°C or lower, and most preferably 260°C or lower.

[0073] The melt flow rate (MFR) of the fluororesin at a temperature (e.g., 265°C or 297°C) within the general molding temperature range of 230 to 350°C is preferably 0.5 g / 10 min or more, more preferably 2.0 g / 10 min or more, even more preferably 5.0 g / 10 min or more, particularly preferably 10 g / 10 min or more, most preferably 15 g / 10 min or more, and preferably 100 g / 10 min or less, more preferably 50 g / 10 min or less, even more preferably 40 g / 10 min or less, and particularly preferably 35 g / 10 min or less. The melt flow rate can be determined, for example, by using a melt indexer to measure the mass (g) of the fluororesin flowing per unit time (10 min) from a nozzle with an inner diameter of 2 mm and a length of 8 mm at a given temperature (e.g., 265°C or 297°C) and a given load (e.g., 2.16 kg or 5 kg).

[0074] The fluororesin is preferably at least one selected from the group consisting of TFE / perfluoro(alkyl vinyl ether) (PAVE) copolymer, tetrafluoroethylene (TFE) / hexafluoropropylene (HFP) copolymer, TFE / ethylene copolymer [ETFE], TFE / ethylene / HFP copolymer, polymers containing CTFE units, and tetrafluoroethylene / hexafluoropropylene / vinylidene fluoride copolymer [THV], more preferably at least one selected from the group consisting of TFE / ethylene copolymer [ETFE], TFE / ethylene / HFP copolymer, and polymers containing CTFE units, and more preferably at least one selected from the group consisting of TFE / ethylene copolymer [ETFE] and TFE / ethylene / HFP copolymer.

[0075] In the present disclosure, the composition of the fluororesin can be calculated by appropriately combining NMR, FT-IR, elemental analysis, and X-ray fluorescence analysis depending on the type of monomer.

[0076] The TFE / HFP copolymer preferably has a TFE / HFP mass ratio of 80-97 / 3-20, more preferably 84-92 / 8-16. The TFE / HFP copolymer may be a binary copolymer consisting of TFE and HFP, or may be a ternary copolymer consisting of TFE and a monomer copolymerizable with HFP (for example, a TFE / HFP / PAVE copolymer).

[0077] The TFE / HFP copolymer is also preferably a TFE / HFP / PAVE copolymer containing polymerized units based on PAVE. The TFE / HFP / PAVE copolymer preferably has a mass ratio of TFE / HFP / PAVE of 70-97 / 2.9-20 / 0.1-10, and more preferably 81-92 / 5-16 / 0.3-5.

[0078] The TFE / PAVE copolymer preferably has a TFE / PAVE mass ratio of 90-99 / 1-10, more preferably 92-97 / 3-8.

[0079] ETFE is a copolymer containing ethylene units and TFE units. ETFE is preferably a copolymer in which the molar ratio of TFE units to ethylene units (TFE units / ethylene units) is 20 / 80 or more and 90 / 10 or less. A more preferred molar ratio is 37 / 63 or more and 85 / 15 or less, and an even more preferred molar ratio is 38 / 62 or more and 80 / 20 or less. The ETFE may be a copolymer consisting of TFE, ethylene, and a monomer copolymerizable with TFE and ethylene. The copolymerizable monomer is a copolymer represented by the following formula: CH2=CX 5 Rf 3 , CF2=CFRf 3 , CF2=CFORf 3 , CH2=C(Rf3 )2 (In the formula, X 5 is H or F, Rf 3 represents a fluoroalkyl group which may contain an ether bond.) Among them, monomers represented by CF2=CFRf 3 , CF2=CFORf 3 and CH2=CX 5 Rf 3 and at least one selected from the group consisting of fluorine-containing vinyl monomers represented by the formula: 4 (In the formula, Rf 4 represents a perfluoroalkyl group having 1 to 5 carbon atoms. 3 is a fluoroalkyl group having 1 to 8 carbon atoms, CH2=CX 5 Rf 3 More preferred is at least one selected from the group consisting of fluorine-containing vinyl monomers represented by the following formula: and HFP is even more preferred. The monomer copolymerizable with TFE and ethylene may be an aliphatic unsaturated carboxylic acid such as itaconic acid or itaconic anhydride. In ETFE, the monomer units copolymerizable with TFE and ethylene preferably account for 0.1 mol % or more, more preferably 0.2 mol % or more, and more preferably 10 mol % or less, more preferably 5 mol % or less, and particularly preferably 4 mol % or less.

[0080] The TFE / ethylene copolymer [ETFE] is also preferably a TFE / ethylene / HFP copolymer containing HFP-based polymerization units (HFP units). The TFE / ethylene / HFP copolymer preferably has a TFE / ethylene / HFP molar ratio of 40-65 / 30-59.5 / 0.5-20, more preferably 40-65 / 30-59.5 / 0.5-10.

[0081] The melting point of ETFE is preferably 160°C or higher, more preferably 170°C or higher, even more preferably 180°C or higher, particularly preferably 190°C or higher, preferably lower than 324°C, more preferably 320°C or lower, even more preferably 300°C or lower, particularly preferably 280°C or lower, and most preferably 260°C or lower.

[0082] The MFR (265°C) of ETFE is preferably 0.5 g / 10 min or more, more preferably 2.0 g / 10 min or more, even more preferably 5.0 g / 10 min or more, particularly preferably 8 g / 10 min or more, most preferably 10 g / 10 min or more, preferably 100 g / 10 min or less, more preferably 50 g / 10 min or less, even more preferably 40 g / 10 min or less, particularly preferably 30 g / 10 min or less, and most preferably 25 g / 10 min or less. The MFR of ETFE is measured at a temperature of 297°C or 265°C and a load of 5 kg.

[0083] It is also suitable to use the ethylene / tetrafluoroethylene copolymer described in JP-A-2019-90013 as ETFE.

[0084] The polymer containing CTFE units is preferably at least one selected from the group consisting of polychlorotrifluoroethylene [PCTFE] and CTFE copolymers.

[0085] The content of CTFE units in a polymer containing CTFE units is preferably 1.0 mol% or more, more preferably 5.0 mol% or more, even more preferably 10.0 mol% or more, particularly preferably 15.0 mol% or more, and is preferably 100 mol% or less, more preferably 75.0 mol% or less, even more preferably 50.0 mol% or less, and particularly preferably 30.0 mol% or less, based on the total monomer units, because low fuel permeability is further improved.

[0086] Examples of polymers containing CTFE units include ethylene / chlorotrifluoroethylene (CTFE) copolymers (ECTFE), polychlorotrifluoroethylene (PCTFE), CTFE / tetrafluoroethylene (TFE) copolymers, and TFE / vinylidene fluoride (VdF) / CTFE copolymers (VTC). At least one selected from the group consisting of PCTFE, ethylene / CTFE copolymers, and CTFE / TFE copolymers is preferred, and CTFE / TFE copolymers are more preferred from the viewpoint of low fuel permeability.

[0087] PCTFE includes CTFE homopolymers and polymers containing CTFE units and minor amounts of comonomer units.

[0088] The melting point of PCTFE is preferably 150° C. or higher, more preferably 190° C. or higher, and preferably 230° C. or lower, more preferably 217° C. or lower. The melting point is the temperature corresponding to the maximum value on the heat of fusion curve when the temperature is increased at a rate of 10° C. / min using a differential scanning calorimeter (DSC).

[0089] The flow value of PCTFE is preferably 1×10 -4 (cm 3 / sec) or more, preferably 5 × 10 -1 (cm 3 The flow value is the volume of resin extruded per second when PCTFE is melted at 230°C using a Koga type flow tester CFT-500D (manufactured by Shimadzu Corporation) and extruded from a nozzle with a diameter of 1 mm under a load of 100 kg.

[0090] The content of CTFE units in PCTFE is preferably 95 mol % or more, more preferably 98 mol % or more, even more preferably 99 mol % or more, and preferably 100 mol % or less.

[0091] The comonomer constituting the comonomer units that can be contained in PCTFE is not particularly limited as long as it is a monomer copolymerizable with CTFE, and examples thereof include TFE, ethylene, vinylidene fluoride, perfluoroalkyl vinyl ether, and hexafluoroethylene.

[0092] Ethylene / CTFE copolymer (ECTFE) is a copolymer containing ethylene units and CTFE units, and preferably contains 46 to 52 mol% of ethylene units and 54 to 48 mol% of CTFE units relative to the total of the ethylene units and CTFE units. ECTFE may be a binary copolymer consisting of only ethylene units and CTFE units, or may further contain polymerized units based on a monomer copolymerizable with ethylene and CTFE (for example, a fluoroalkyl vinyl ether (PAVE) derivative). The content of polymerized units based on monomers copolymerizable with ethylene and CTFE is preferably 0.01 mol % or more and 5 mol % or less based on the total of ethylene units, CTFE units, and polymerized units based on the above-mentioned copolymerizable monomers.

[0093] The MFR (230°C) of ECTFE is preferably 0.5 g / 10 min or more and preferably 100 g / 10 min or less. The MFR of ECTFE is measured at a temperature of 230°C and a load of 2.16 kg.

[0094] The CTFE / TFE copolymer contains CTFE units and TFE units. Particularly preferred CTFE / TFE copolymers include those containing CTFE units, TFE units, and monomer (α) units derived from a monomer (α) copolymerizable with these units.

[0095] The monomer (α) is not particularly limited as long as it is a monomer copolymerizable with CTFE and TFE, and examples thereof include ethylene (Et), VdF, CF₂=CF-ORf 1 (In the formula, Rf 1 perfluoro(alkyl vinyl ether) [PAVE] represented by a perfluoroalkyl group having 1 to 8 carbon atoms, CX 3 X4 =CX 5 (CF2) n X 6 (In the formula, X 3 , X 4 and X 5 are the same or different and are a hydrogen atom or a fluorine atom; X 6 is a hydrogen atom, a fluorine atom, or a chlorine atom; n is an integer of 1 to 10), a vinyl monomer represented by CF2=CF-OCH2-Rf 2 (In the formula, Rf 2 and alkyl perfluorovinyl ether derivatives represented by the formula (wherein is a perfluoroalkyl group having 1 to 5 carbon atoms), and among these, at least one selected from the group consisting of PAVE, the vinyl monomers and alkyl perfluorovinyl ether derivatives is preferred, and at least one selected from the group consisting of PAVE and HFP is more preferred.

[0096] For PAVE, CF2 = CF-ORf 3 (In the formula, Rf 3 represents a perfluoroalkyl group having 1 to 5 carbon atoms.) is preferred, and examples thereof include perfluoro(methyl vinyl ether) [PMVE], perfluoro(ethyl vinyl ether) [PEVE], perfluoro(propyl vinyl ether) [PPVE], and perfluoro(butyl vinyl ether). Among these, at least one selected from the group consisting of PMVE, PEVE, and PPVE is more preferred, and PPVE is even more preferred.

[0097] As alkyl perfluorovinyl ether derivatives, Rf 2 is preferably a perfluoroalkyl group having 1 to 3 carbon atoms, and CF2=CF-OCH2-CF2CF3 is more preferred.

[0098] The ratio of CTFE units to TFE units in the CTFE / TFE copolymer is preferably 15.0 to 90.0 mol % for CTFE units and 85.0 to 10.0 mol % for TFE units, more preferably 15.0 to 50.0 mol % for CTFE units and 85.0 to 50.0 mol % for TFE units, and even more preferably 15.0 to 30.0 mol % for CTFE units and 85.0 to 70.0 mol % for TFE units.

[0099] The CTFE / TFE copolymer preferably contains 90.0 to 99.9 mol% of CTFE units and TFE units in total, and 0.1 to 10.0 mol% of monomer (α) units. If the monomer (α) unit content is less than 0.1 mol%, the copolymer tends to be inferior in moldability, environmental stress cracking resistance, and fuel cracking resistance, while if it exceeds 10.0 mol%, the copolymer tends to be inferior in fuel barrier properties, heat resistance, and mechanical properties.

[0100] As the CTFE / TFE copolymer, a CTFE / TFE / PAVE copolymer is particularly preferred.

[0101] In the CTFE / TFE / PAVE copolymer, the PAVE may be perfluoro(methyl vinyl ether) [PMVE], perfluoro(ethyl vinyl ether) [PEVE], perfluoro(propyl vinyl ether) [PPVE], or perfluoro(butyl vinyl ether), and among these, at least one selected from the group consisting of PMVE, PEVE, and PPVE is preferred, with PPVE being more preferred. In the CTFE / TFE / PAVE copolymer, the PAVE units preferably account for 0.5 mol % or more and 5 mol % or less of all monomer units.

[0102] The melting point of the CTFE / TFE copolymer is preferably 190°C or higher, more preferably 210°C or higher, even more preferably 220°C or higher, particularly preferably 230°C or higher, and most preferably 240°C or higher; it is preferably lower than 324°C, more preferably 320°C or lower, even more preferably 270°C or lower, and most preferably 260°C or lower.

[0103] The MFR (297°C) of the CTFE / TFE copolymer is preferably 0.5 g / 10 min or more, more preferably 2.0 g / 10 min or more, even more preferably 5.0 g / 10 min or more, particularly preferably 7 g / 10 min or more, most preferably 10 g / 10 min or more, and preferably 100 g / 10 min or less, more preferably 50 g / 10 min or less, even more preferably 40 g / 10 min or less, and particularly preferably 35 g / 10 min or less. The MFR of the CTFE / TFE copolymer is measured at a temperature of 297°C and a load of 5 kg.

[0104] The fluororesin layer (F) preferably has electrical conductivity. When the fluororesin layer (F) has electrical conductivity, it can prevent the laminate from being charged even when static electricity is generated due to friction between the laminate and fuel.

[0105] The fluororesin layer (F) preferably contains a conductive filler, which easily imparts conductivity to the fluororesin layer (F), thereby preventing the laminate from becoming charged even when static electricity is generated by friction between the laminate and fuel.

[0106] As the conductive filler, the same conductive filler as that which can be contained in the conductive layer (N1) can be used, and the same conductive filler is preferred.

[0107] The amount of conductive filler to be added is determined appropriately based on the type of fluororesin, the conductive performance required of the laminate, molding conditions, etc., but is preferably 1 part by mass or more and 30 parts by mass or less per 100 parts by mass of fluororesin, with a more preferred lower limit of 5 parts by mass and a more preferred upper limit of 20 parts by mass.

[0108] In addition to the conductive filler, the fluororesin layer (F) may contain various additives such as a reinforcing agent, a bulking agent, an ultraviolet absorber, a pigment, etc., within the scope of the object of the present disclosure. By using such additives, the properties of the fluororesin layer (F), such as surface hardness, abrasion resistance, anti-static property, and weather resistance, can be improved.

[0109] When the laminate of the present disclosure includes a fluororesin layer (F), the fluororesin layer (F) is preferably configured to come into contact with fuel. By forming the contact surface between the laminate and fuel with the fluororesin layer (F), the laminate is endowed with excellent fuel resistance and the durability of the laminate is improved. Furthermore, when the fluororesin layer (F) is conductive, by forming the contact surface between the laminate and fuel with the fluororesin layer (F), charging of the laminate can be further prevented even when static electricity is generated due to friction between the laminate and fuel.

[0110] (Non-fluorinated polymer (N2)) The laminate of the present disclosure may further include a non-fluorinated polymer layer (N2) that is not electrically conductive and contains a non-fluorinated polymer (N2) (excluding the non-fluorinated polymer (A)). The non-fluorinated polymer (N2) is a non-fluorinated polymer other than an ethylene / vinyl alcohol copolymer and an aromatic polyamide.

[0111] A wide range of polymers known as thermoplastic resins other than ethylene / vinyl alcohol copolymers and aromatic polyamides can be used as the non-fluorinated polymer (N2), including aliphatic polyamide resins, polyolefin resins, vinyl chloride resins, polyurethane resins, polyester resins, polyaramid resins, polyimide resins, polyamide-imide resins, polyphenylene oxide resins, polyacetal resins, polycarbonate resins, acrylic resins, styrene resins, acrylonitrile / butadiene / styrene resins (ABS), cellulose resins, polyether ether ketone resins (PEEK), polysulfone resins, polyethersulfone resins (PES), polyetherimide resins, polyphenylene sulfide resins, polybutylene naphthalate resins, polybutylene terephthalate resins, and polyphthalamide (PPA).

[0112] The melting point of the non-fluorinated polymer (N2) is preferably 50°C or higher, more preferably 100°C or higher, even more preferably 150°C or higher, and preferably 400°C or lower, more preferably 300°C or lower, even more preferably 250°C or lower.

[0113] As the non-fluorinated polymer (N2), at least one selected from the group consisting of aliphatic polyamide resins and polyolefin resins is preferred, and aliphatic polyamide resins are more preferred.

[0114] Aliphatic polyamide resins are so-called nylon resins made of polymers in which an amide bond in the molecule is bonded to an aliphatic structure or an alicyclic structure.

[0115] The aliphatic polyamide resin (nylon resin) is not particularly limited, and examples thereof include polyamide 6, polyamide 66, polyamide 11, polyamide 12, polyamide 610, polyamide 1010, polyamide 612, polyamide 6 / 66, polyamide 66 / 12, polyamide 46, metaxylylenediamine / adipic acid copolymer, polyamide 62, polyamide 92, polyamide 122, and polyamide 142.

[0116] Aliphatic polyamide resins may also be polymers in which a repeating unit that does not contain an amide bond is block- or graft-copolymerized into a portion of the molecule. Examples of such aliphatic polyamide resins include polyamide elastomers such as polyamide 6 / polyester copolymer, polyamide 6 / polyether copolymer, polyamide 12 / polyester copolymer, and polyamide 12 / polyether copolymer. These polyamide elastomers are obtained by block copolymerization of a polyamide oligomer and a polyester oligomer via an ester bond, or by block copolymerization of a polyamide oligomer and a polyether oligomer via an ether bond. Examples of the polyester oligomer include polycaprolactone and polyethylene adipate, and examples of the polyether oligomer include polyethylene glycol, polypropylene glycol, and polytetramethylene glycol. Examples of the polyamide elastomers include polyamide 6 / polytetramethylene glycol copolymer and polyamide 12 / polytetramethylene glycol copolymer.

[0117] As the aliphatic polyamide resin, at least one selected from the group consisting of polyamide 6, polyamide 66, polyamide 11, polyamide 12, polyamide 610, polyamide 1010, polyamide 612, polyamide 62, polyamide 6 / 66, polyamide 66 / 12, polyamide 6 / polyester copolymer, polyamide 6 / polyether copolymer, polyamide 12 / polyester copolymer and polyamide 12 / polyether copolymer is preferred, since a layer made of the aliphatic polyamide resin can obtain sufficient mechanical strength even when it is a thin layer, and at least one selected from the group consisting of polyamide 11, polyamide 12 and polyamide 612 is more preferred.

[0118] The polyolefin resin is a resin having monomer units derived from a vinyl group-containing monomer that does not contain a fluorine atom.

[0119] The polyolefin resin is not particularly limited, and examples thereof include polyolefins such as polyethylene, polypropylene, high-density polyolefins, and low-density polyolefins, as well as modified polyolefins obtained by modifying the above polyolefins with maleic anhydride or the like, epoxy-modified polyolefins, and amine-modified polyolefins, with high-density polyolefins being preferred.

[0120] The non-fluorinated polymer layer (N2) may contain additives other than the conductive filler, such as various additives such as reinforcing agents, bulking agents, UV absorbers, pigments, etc., within the scope of the present disclosure. The use of such additives can improve the properties of the non-fluorinated polymer layer (N2), such as surface hardness, abrasion resistance, anti-static properties, and weather resistance.

[0121] The non-fluorinated polymer layer (N2) is not electrically conductive and does not contain a conductive filler.

[0122] (Laminated body configuration) The laminate of the present disclosure includes at least a non-fluorinated polymer layer (A) containing at least one non-fluorinated polymer (A) selected from the group consisting of an ethylene / vinyl alcohol copolymer and an aromatic polyamide. The number of layers of the laminate of the present disclosure is not particularly limited as long as it is 2 or more. The number of layers of the laminate of the present disclosure may be 2 to 5.

[0123] The laminate of the present disclosure may include, in addition to the non-fluorinated polymer layer (A), a polymer-containing polymer layer (B) (excluding the non-fluorinated polymer layer (A)). Examples of the polymer layer (B) include a conductive layer (N1), a fluororesin layer (F), and a non-fluorinated polymer layer (N2).

[0124] In the laminate of the present disclosure, the non-fluorinated polymer layer (A) and the polymer layer (B) may be bonded directly or via another layer such as an adhesive layer, but are preferably bonded directly.

[0125] The laminate of the present disclosure includes a laminate comprising at least a conductive layer (N1) and a non-fluorinated polymer layer (A), and a laminate comprising at least a fluororesin layer (F) and a non-fluorinated polymer layer (A).

[0126] The laminate of the present disclosure includes, for example, a laminate having an electrically conductive layer (N1) / a non-fluorinated polymer layer (A) as the innermost layer / an outermost layer, a laminate having a fluororesin layer (F) / a non-fluorinated polymer layer (A); a laminate comprising an electrically conductive layer (N1), a non-fluorinated polymer layer (A), and a non-fluorinated polymer layer (N2) as the innermost layer, middle layer, and outermost layer, a laminate comprising a fluororesin layer (F), a non-fluorinated polymer layer (A), and a non-fluorinated polymer layer (N2); a laminate comprising an electrically conductive layer (N1) / a non-fluorinated polymer layer (N2) / a non-fluorinated polymer layer (A) / a non-fluorinated polymer layer (N2) as the innermost layer / intermediate layer / outermost layer, a laminate comprising a fluororesin layer (F) / a non-fluorinated polymer layer (N2) / a non-fluorinated polymer layer (A) / a non-fluorinated polymer layer (N2); a laminate comprising, as the innermost layer / inner layer / intermediate layer / outer layer / outermost layer, a conductive layer (N1) / a non-fluorinated polymer layer (N2) / a non-fluorinated polymer layer (A) / a non-fluorinated polymer layer (N2) / a non-fluorinated polymer layer (N2); a laminate comprising, as the innermost layer / inner layer / intermediate layer / outer layer / outermost layer, a conductive layer (N1) / a non-fluorinated polymer layer (N2) / a non-fluorinated polymer layer (A) / a non-fluorinated polymer layer (N2) / a non-fluorinated polymer layer (N2); Examples include:

[0127] When the laminate of the present disclosure comprises two or more non-fluorinated polymer layers (A), the type of non-fluorinated polymer (A) contained in each layer may be the same or different. When the laminate of the present disclosure comprises two or more conductive layers (N1), the type of non-fluorinated polymer (N1) contained in each layer may be the same or different. When the laminate of the present disclosure comprises two or more fluororesin layers (F), the type of fluororesin contained in each layer may be the same or different. When the laminate of the present disclosure comprises two or more non-fluorinated polymer layers (N2), the type of non-fluorinated polymer (N2) contained in each layer may be the same or different. In the laminate of the present disclosure, the boundary between adjacent layers does not necessarily need to be clear, and the molecular chains of the polymers constituting each layer may interpenetrate from the contacting surfaces, resulting in a layer structure with a concentration gradient.

[0128] The laminate of the present disclosure may have other layers. The thickness, shape, etc. of each layer of the laminate of the present disclosure may be appropriately selected depending on the purpose of use, the form of use, etc.

[0129] The fuel permeation rate of the laminate of the present disclosure is preferably 15 g / m 2 / day or less, and more preferably 10 g / m 2 / day or less, and more preferably 5.0 g / m 2 / day or less, and particularly preferably 3.0 g / m 2 / day or less. When the fuel contains alcohol, the fuel permeation rate of the laminate of the present disclosure is preferably 15 g / m 2 / day or less, and more preferably 10 g / m 2 / day or less, and more preferably 5.0 g / m 2 / day or less, and particularly preferably 3.0 g / m 2 / day or less. When the fuel contains gasoline, the fuel permeation rate of the laminate of the present disclosure is preferably 15 g / m 2 / day or less, and more preferably 10 g / m 2 / day or less, and more preferably 5.0 g / m 2 / day or less, and particularly preferably 3.0 g / m 2 / day or less. When the fuel contains diesel fuel (light oil), the fuel permeation rate of the laminate of the present disclosure is preferably 8.0 g / m 2 / day or less, more preferably 5.0 g / m 2 / day or less, and more preferably 3.0 g / m 2 / day or less.

[0130] The fuel permeation rate of the laminate is the rate at which a fuel containing at least compound (1) consisting only of carbon, hydrogen, and oxygen atoms and having a carbonyl group or an ether bond permeates the laminate. The fuel permeation rate of the laminate can be determined by fabricating a tubular laminate, preparing a fuel containing compound (1) at a predetermined concentration, sealing the fuel in the tubular laminate, leaving it at 60°C or 80°C, measuring the mass change per hour, and calculating the fuel permeation rate from the mass change and the internal area of ​​the tubular laminate. When the fuel contains alcohol or gasoline, the fuel can be sealed in the tubular laminate and left at 60°C, after which the mass change per hour can be measured. When the fuel contains diesel fuel (light oil), the fuel can be sealed in the tubular laminate and left at 80°C, after which the mass change per hour can be measured.

[0131] The laminate of the present disclosure can be formed into various shapes such as a film, a sheet, a tube (hose), a bottle, or a tank. The film, sheet, tube, or hose shape may be corrugated, corrugated, or convoluted. The laminate of the present disclosure may be, for example, a film, a sheet, a tube, a hose, a bottle, a container, or a tank. The laminate of the present disclosure can be suitably used for, for example, fuel tubes or hoses such as automobile fuel tubes or automobile fuel hoses, underground tubes or hoses for fuel supply facilities, automobile fuel tanks, and various automobile seals such as O-rings for fuel pumps.

[0132] In one embodiment, the laminate of the present disclosure is used as a component constituting a system for distributing fuel, the system comprising at least a compound (1) consisting only of carbon atoms, hydrogen atoms, and oxygen atoms and having a carbonyl group or an ether bond. The system for distributing fuel is, for example, a system used for storing or supplying fuel. Components used in such systems include tanks, tubes, hoses, caps, valves, diaphragms, seals (O-rings), and the like. The system for distributing fuel is used, for example, not only in automobiles but also in facilities for supplying fuel to automobile fuel tanks. A typical example of a component constituting a system for distributing fuel is a fuel tube or a fuel hose.

[0133] (Tubes and Hoses) The laminate of the present disclosure can be suitably used as a tube or a hose. In this disclosure, the term "tube or hose" includes articles generally called tubes or hoses, and is usually an article having a shape capable of transporting a fluid. In this disclosure, the term "tube or hose" does not imply that a tube and a hose are different articles.

[0134] The tube or hose of the present disclosure can have the same construction as the laminate described above.

[0135] The tube or hose of the present disclosure preferably has a fuel permeation rate of 15 g / m 2 / day or less, and more preferably 10 g / m 2 / day or less, and more preferably 5.0 g / m 2 / day or less, and particularly preferably 3.0 g / m 2 / day or less. When the fuel contains alcohol, the fuel permeation rate of the tube or hose of the present disclosure is preferably 15 g / m 2 / day or less, and more preferably 10 g / m 2 / day or less, and more preferably 5.0 g / m 2 / day or less, and particularly preferably 3.0 g / m 2 / day or less. When the fuel contains gasoline, the fuel permeation rate of the tube or hose of the present disclosure is preferably 15 g / m 2 / day or less, and more preferably 10 g / m 2 / day or less, and more preferably 5.0 g / m 2 / day or less, and particularly preferably 3.0 g / m 2 / day or less. When the fuel contains diesel fuel (gas oil), the fuel permeation rate of the tube or hose of the present disclosure is preferably 8.0 g / m 2 / day or less, more preferably 5.0 g / m 2 / day or less, and more preferably 3.0 g / m 2 / day or less.

[0136] The fuel permeation rate of a tube or hose is the rate at which a fuel containing at least compound (1), consisting only of carbon, hydrogen, and oxygen atoms and having a carbonyl group or an ether bond, permeates the tube or hose. The fuel permeation rate of a tube or hose can be determined by preparing a fuel containing compound (1) at a predetermined concentration, sealing the fuel in the tube or hose, leaving it at 60°C or 80°C, measuring the mass change per hour, and calculating the fuel permeation rate from the mass change and the inner area of ​​the tube or hose. When the fuel contains alcohol or gasoline, the fuel can be sealed in the tube or hose and left at 60°C, and the mass change per hour can be measured. When the fuel contains diesel fuel (light oil), the fuel can be sealed in the tube or hose and left at 80°C, and the mass change per hour can be measured.

[0137] The outer diameter of the tube or hose is preferably 2 mm or more, more preferably 3 mm or more, even more preferably 4 mm or more, and most preferably 6 mm or more, and is preferably 20 mm or less, more preferably 18 mm or less, even more preferably 16 mm or less, and most preferably 14 mm or less.

[0138] The inner diameter of the tube or hose is preferably 1 mm or more, more preferably 2 mm or more, even more preferably 3 mm or more, and most preferably 4 mm or more, and is preferably 15 mm or less, more preferably 13 mm or less, even more preferably 11 mm or less, and most preferably 10 mm or less.

[0139] The thickness of the tube or hose (the difference between the outer diameter and the inner diameter) is preferably 0.5 mm or more, more preferably 0.6 mm or more, even more preferably 0.7 mm or more, and preferably 8 mm or less, more preferably 6 mm or less, even more preferably 4 mm or less, and particularly preferably 2 mm or less.

[0140] The thickness of the non-fluorinated polymer layer (A) in the laminate and the tube or the hose is preferably 0.05 mm or more, more preferably 0.10 mm or more, even more preferably 0.15 mm or more, and is preferably 0.40 mm or less, more preferably 0.30 mm or less, even more preferably 0.20 mm or less. When the laminate and the tube or the hose have two or more non-fluorinated polymer layers (A), the thickness of the non-fluorinated polymer layer (A) is the total thickness of the layers.

[0141] The thickness of the polymer layer (B) in the laminate and the tube or hose is preferably 0.10 mm or more, more preferably 0.20 mm or more, even more preferably 0.30 mm or more, and preferably 0.90 mm or less, more preferably 0.80 mm or less, and even more preferably 0.70 mm or less. When the laminate and the tube or hose have two or more polymer layers (B), the thickness of the polymer layer (B) is the total thickness of the layers.

[0142] The thickness of the conductive layer (N1) in the laminate and the tube or hose is preferably 0.05 mm or more, more preferably 0.10 mm or more, and preferably 0.40 mm or less, more preferably 0.30 mm or less, and even more preferably 0.20 mm or less. When the laminate and the tube or hose have two or more conductive layers (N1), the thickness of the conductive layer (N1) is the total thickness of the layers.

[0143] The thickness of the fluororesin layer (F) in the laminate and the tube or hose is preferably 0.05 mm or more, more preferably 0.10 mm or more, and preferably 0.40 mm or less, more preferably 0.30 mm or less, and even more preferably 0.20 mm or less. When the laminate and the tube or hose have two or more fluororesin layers (F), the thickness of the fluororesin layer (F) is the total thickness of the layers.

[0144] The thickness of the non-fluorinated polymer layer (N2) in the laminate and the tube or hose is preferably 0.10 mm or more, more preferably 0.20 mm or more, even more preferably 0.30 mm or more, and preferably 0.90 mm or less, more preferably 0.80 mm or less, and even more preferably 0.70 mm or less. When the laminate and the tube or hose have two or more non-fluorinated polymer layers (N2), the thickness of the non-fluorinated polymer layer (N2) is the total thickness of the layers.

[0145] The tube or hose may be corrugated, corrugated, convoluted, etc. When the tube or hose has a corrugated shape, it has an area where multiple corrugated folds are arranged in a circular pattern, which allows one side of the ring to be compressed and the other side to be stretched outward in that area, making it possible to easily bend it to any angle without stress fatigue or delamination.

[0146] There is no particular limitation on the method for forming the corrugated region, but it can be easily formed by forming a straight tube or hose, followed by molding or the like to form a predetermined corrugated shape or the like.

[0147] The method for producing the laminate of the present disclosure includes, for example, (1) A method of forming a multilayer laminate in one step by co-extrusion molding the polymers that form each layer, thereby heat-sealing (melting and bonding) the layers together (co-extrusion molding). (2) A method in which each layer is produced separately using an extruder and then laminated together, and the layers are bonded together by heat fusion. (3) A method of forming a laminate by extruding a polymer that will form a layer adjacent to a previously prepared layer onto the surface of the previously prepared layer using an extruder; (4) A method in which a polymer that will form a layer adjacent to a previously prepared layer is electrostatically coated on the surface of the layer, and then the resulting coated object is heated either overall or from the coated side to heat and melt the coated polymer and form a layer. etc.

[0148] When the laminate of the present disclosure is a tube or a hose, examples of the method corresponding to (2) above include (2a) a method in which each cylindrical layer is formed separately using an extruder, and a layer that will come into contact with the layer that will become the inner layer is coated with a heat-shrinkable tube; a method corresponding to (3) above includes (3a) a method in which the layer that will become the inner layer is first formed using an inner layer extruder, and a layer that will come into contact with the inner layer is formed on the outer surface of the inner layer using an outer layer extruder; and a method corresponding to (4) above includes (4a) a method in which the polymer that will make up the inner layer is electrostatically coated on the inside of the layer that will come into contact with the inner layer, and the resulting coated article is placed in a heating oven and heated overall, or a rod-shaped heating device is inserted inside a cylindrical coated article and heated from the inside, thereby heating and melting the polymer that will make up the inner layer and molding it.

[0149] If the layers constituting the laminate and tube or hose of the present disclosure are co-extrudable, they are generally formed by the co-extrusion molding method (1) above. Examples of the co-extrusion molding include conventionally known multilayer co-extrusion manufacturing methods such as the multi-manifold method and the feed block method.

[0150] In the molding methods (2) and (3) above, after each layer is formed, the contact surface of each layer with other layers may be surface-treated to enhance interlayer adhesion. Examples of such surface treatments include etching treatments such as sodium etching, corona treatments, and plasma treatments such as low-temperature plasma treatments.

[0151] The laminate of the present disclosure can also be formed by laminating multiple materials in multiple stages using rotational molding. In this case, the melting point of the outer layer material does not necessarily have to be higher than that of the inner layer material; the melting point of the inner layer material may be 100°C or more higher than that of the outer layer material. In this case, it is preferable to have a heating section inside as well.

[0152] The tube or hose of the present disclosure can be suitably used, for example, as a fuel tube or hose such as an automobile fuel tube or hose, or as an underground tube or hose for a fuel supply facility.

[0153] Although the embodiments have been described above, it will be understood that various changes in form and details can be made without departing from the spirit and scope of the claims.

[0154] <1> According to a first aspect of the present disclosure, A laminate in contact with fuel, comprising: The fuel contains at least a compound (1) consisting of only carbon atoms, hydrogen atoms, and oxygen atoms and having a carbonyl group or an ether bond; The laminate includes at least a non-fluorinated polymer layer containing at least one non-fluorinated polymer selected from the group consisting of ethylene / vinyl alcohol copolymers and aromatic polyamides. <2> According to a second aspect of the present disclosure, There is provided a laminate according to a first aspect, wherein the compound (1) is at least one selected from the group consisting of a carbonate ester, a chain ether, and a cyclic ether. <3> According to a third aspect of the present disclosure, There is provided a laminate according to the first or second aspect, wherein compound (1) is at least one selected from the group consisting of dimethyl carbonate, diethyl carbonate, dimethyl ether, methyl tert-butyl ether, oxymethylene dimethyl ether and 1,3 dioxolane. <4> According to a fourth aspect of the present disclosure, There is provided a laminate according to any one of the first to third aspects, wherein the fuel further contains alcohol. <5> According to a fifth aspect of the present disclosure, There is provided a laminate according to any one of the first to fourth aspects, wherein the fuel further contains gasoline. <6> According to a sixth aspect of the present disclosure, There is provided a laminate according to any one of the first to fifth aspects, wherein the fuel further contains diesel fuel. <7> According to a seventh aspect of the present disclosure, There is provided a laminate according to any one of the first to sixth aspects, wherein the content of compound (1) in the fuel is 0.1 to 20% by volume. <8> According to an eighth aspect of the present disclosure, There is provided a laminate according to any one of the first to seventh aspects, wherein the non-fluorinated polymer layer has a thickness of 0.05 to 0.40 mm. <9> According to a ninth aspect of the present disclosure, There is provided a laminate according to any one of the first to eighth aspects, which further comprises a conductive layer having electrical conductivity and containing a non-fluorinated polymer. <10> According to a tenth aspect of the present disclosure, In a ninth aspect, there is provided a laminate, wherein the non-fluorinated polymer is an aromatic polyamide. <11> According to an eleventh aspect of the present disclosure, In accordance with the ninth or tenth aspect, there is provided a laminate in which the conductive layer is in contact with the fuel. <12> According to a twelfth aspect of the present disclosure, There is provided a laminate according to any one of the first to eleventh aspects, further comprising a fluororesin layer containing a fluororesin. <13> According to a thirteenth aspect of the present disclosure, There is provided a laminate according to a twelfth aspect, wherein the fluororesin is at least one selected from the group consisting of fluororesins containing ethylene units and tetrafluoroethylene units, and fluororesins containing chlorotrifluoroethylene units and tetrafluoroethylene units. <14> According to a fourteenth aspect of the present disclosure, According to a twelfth or thirteenth aspect, there is provided a laminate, wherein the fluororesin layer has electrical conductivity. <15> According to a fifteenth aspect of the present disclosure, According to any one of the twelfth to fourteenth aspects, there is provided a laminate, wherein the fluororesin layer comes into contact with the fuel. <16> According to a sixteenth aspect of the present disclosure, The fuel permeation rate is 15 g / m 2 The laminate according to any one of the first to fifteenth aspects is provided, in which the drying time is 1 / day or less. <17> According to a seventeenth aspect of the present disclosure, There is provided a tube or hose formed from the laminate according to any one of the first to sixteenth aspects. <18> According to an eighteenth aspect of the present disclosure, A tube or hose formed from the laminate according to any one of the first to eleventh and sixteenth aspects, The laminate is a conductive layer (N1) containing a conductive filler and an aromatic polyamide; a non-fluorinated polymer layer (A) containing an aromatic polyamide, and Non-fluorinated polymer layer (N2) containing aliphatic polyamide resin In this order, The conductive layer (N1) is the innermost layer and is in contact with the fuel. A tube or hose is provided. <19> According to a nineteenth aspect of the present disclosure, A tube or hose formed from the laminate according to any one of the first to eighth and twelfth to sixteenth aspects, The laminate is a fluororesin layer (F) containing a conductive filler and a fluororesin containing an ethylene unit and a tetrafluoroethylene unit; a non-fluorinated polymer layer (N2) containing an aliphatic polyamide resin; a non-fluorinated polymer layer (A) containing an ethylene / vinyl alcohol copolymer; a non-fluorinated polymer layer (N2) containing an aliphatic polyamide resin, and Non-fluorinated polymer layer (N2) containing aliphatic polyamide resin In this order, The fluororesin layer (F) is the innermost layer and comes into contact with the fuel. A tube or hose is provided. [Example]

[0155] Next, embodiments of the present disclosure will be described with reference to examples, but the present disclosure is not limited to these examples.

[0156] The values ​​in the examples were measured by the following methods.

[0157] <Polymer composition (monomer composition of fluororesin)> Using a nuclear magnetic resonance spectrometer AC300 (manufactured by Bruker-Biospin), 19 F-NMR measurements were performed, and the monomer composition of the fluororesin (the content of each monomer unit in the polymer) was determined from the integral value of each peak. Depending on the type of monomer, the results of elemental analysis were appropriately combined to determine the monomer composition of the fluororesin.

[0158] <Melting point> Using a differential scanning calorimeter RDC220 (Seiko Instruments), heat measurement was carried out at a temperature rise rate of 10°C / min in accordance with ASTM D 4591, and the melting point of the fluororesin was determined from the peak of the obtained endothermic curve.

[0159] <Melt flow rate (MFR)> Using a melt indexer (manufactured by Yasuda Seiki Seisakusho Co., Ltd.), the mass of fluororesin flowing out per 10 minutes (g / 10 min) from a nozzle with an inner diameter of 2 mm and a length of 8 mm was determined in accordance with ASTM D 1238 at 265°C or 297°C under a load of 5 kg, and was taken as MFR.

[0160] <Fuel permeation rate> The tubes obtained in the experimental and comparative experimental examples were cut and their inner diameters and lengths were measured. Swagelok fittings were attached to both ends of the tube, the tube was filled with the following fuels, the lid was tightened, and the mass of the tube with the fuel sealed inside was measured. The tube was then kept at 60°C or 80°C, and the mass was measured after 1000 hours had elapsed. The mass loss was calculated from each measured mass, and the fuel permeation rate (g / m) was calculated from the mass loss and the inner area of ​​the tube. 2 / day) was calculated.

[0161] The fuel permeation rate was measured using the following fuels, each containing a random ratio of CE10 (toluene / isooctane / ethanol = 45 / 45 / 10% by volume), CM15 (toluene / isooctane / methanol = 42.5 / 42.5 / 15% by volume), Fuel C (toluene / isooctane = 50 / 50% by volume), E (ethanol), M (methanol), and DMC (dimethyl carbonate). When using these fuels, the tube was kept at 60°C, and the mass was measured after 1000 hours to calculate the fuel permeation rate. Fuel (1): CE10 100% by volume Fuel (2): Fuel C / E / DMC = 85 / 10 / 5 (volume%) Fuel (3): Fuel C / E / DMC = 80 / 10 / 10 (volume%) Fuel (4): Fuel C / E / DMC = 70 / 10 / 20 (volume%) Fuel (5): E / DMC = 10 / 90 (volume%) Fuel (6): DMC 100% by volume Fuel (7): CM15 100% by volume Fuel (8): Fuel C / M / DMC = 65 / 15 / 20 (volume%)

[0162] The fuel permeation rate was measured using the following fuels containing diesel and DMC (dimethyl carbonate) in arbitrary proportions. When using these fuels, the tube was kept at 80°C, and the mass was measured after 1000 hours to calculate the fuel permeation rate. Fuel (1): Diesel 100% by volume Fuel (2): diesel / DMC = 95 / 5 (volume%) Fuel (3): diesel / DMC = 90 / 10 (volume%) Fuel (4): diesel / DMC = 80 / 20 (volume%)

[0163] The following materials were used in the experimental examples and comparative experimental examples.

[0164] Conductive Polyamide 9T (PA9T cond.) Kuraray, Genestar TS341 Polyamide 9T (PA9T) Kuraray, Genestar N1001D

[0165] Fluorine Resin A Polymer composition (mol%): TFE / Et / HFP / 2,3,3,4,4,5,5-heptafluoro-1-pentene = 45.5 / 44.4 / 9.5 / 0.6 Melting point: 197℃ Melt flow rate (265℃): 5.0g / 10min Carbon black content: 12% by mass

[0166] Ethylene / vinyl alcohol copolymer (EVOH) Kuraray, F101B

[0167] Polyamide 12 (PA12) Polypla-Evonik, Daiamid X7297 Polyamide 612 (PA612) Evonik VESTAMID SX8002

[0168] Experimental Examples 1 and 2 and Comparative Experimental Example 1 Using a five-type, five-layer tube extrusion device (manufactured by Plastics Engineering Research Institute) equipped with a multi-manifold, each material was supplied to the extruder so that each layer was composed of the material listed in Table 1, and a multi-layer tube with an outer diameter of 8 mm and an inner diameter of 6 mm was molded.

[0169] The physical properties of the resulting multilayer tube were measured by the methods described above. The results are shown in Table 2.

[0170] [Table 1]

[0171] [Table 2]

[0172] Experimental Examples 3-4 and Comparative Experimental Examples 2-3 Using a five-type, five-layer tube extrusion device (manufactured by Plastics Engineering Research Institute) equipped with a multi-manifold, each material was supplied to the extruder so that each layer was composed of the material listed in Table 1, and a multi-layer tube with an outer diameter of 8 mm and an inner diameter of 6 mm was molded.

[0173] The physical properties of the resulting multilayer tube were measured by the methods described above. The results are shown in Table 2.

[0174] [Table 3]

[0175] [Table 4]

Claims

1. A laminate in contact with fuel, comprising: The fuel contains at least a compound (1) consisting of only carbon atoms, hydrogen atoms, and oxygen atoms and having a carbonyl group or an ether bond; Compound (1) is at least one selected from the group consisting of dimethyl carbonate and diethyl carbonate, The laminate comprises at least a non-fluorinated polymer layer containing at least one non-fluorinated polymer selected from the group consisting of ethylene / vinyl alcohol copolymers and semi-aromatic polyamides.

2. 10. The laminate of claim 1, wherein the fuel further comprises an alcohol.

3. 3. The laminate according to claim 1, wherein the fuel further comprises gasoline.

4. 3. The laminate according to claim 1, wherein the fuel further comprises diesel fuel.

5. 3. The laminate according to claim 1, wherein the content of the compound (1) in the fuel is 0.1 to 20% by volume.

6. 3. The laminate according to claim 1, wherein the non-fluorinated polymer layer has a thickness of 0.05 to 0.40 mm.

7. 3. The laminate according to claim 1, further comprising a conductive layer having electrical conductivity and containing a non-fluorinated polymer.

8. 8. The laminate of claim 7, wherein the non-fluorinated polymer in the conductive layer is an aromatic polyamide.

9. 8. The stack of claim 7, wherein the conductive layer contacts the fuel.

10. The laminate according to claim 1 or 2, further comprising a fluororesin layer containing a fluororesin.

11. 11. The laminate according to claim 10, wherein the fluororesin is at least one selected from the group consisting of fluororesins containing ethylene units and tetrafluoroethylene units, and fluororesins containing chlorotrifluoroethylene units and tetrafluoroethylene units.

12. The laminate according to claim 10 , wherein the fluororesin layer is electrically conductive.

13. The laminate according to claim 10 , wherein the fluororesin layer is in contact with the fuel.

14. The fuel permeation rate is 15 g / m ２ 3. The laminate according to claim 1, wherein the average particle size is 1 / day or less.

15. A tube or hose formed from the laminate of claim 1 or 2.

16. A tube or hose formed from the laminate of claim 1 or 2, The laminate is a conductive layer (N1) containing a conductive filler and an aromatic polyamide; a non-fluorinated polymer layer (A) containing a semi-aromatic polyamide, and a non-fluorinated polymer layer (N2) containing an aliphatic polyamide resin; In this order, The conductive layer (N1) is the innermost layer and is in contact with the fuel. Tube or hose.

17. A tube or hose formed from the laminate of claim 1 or 2, The laminate is a fluororesin layer (F) containing a conductive filler and a fluororesin containing an ethylene unit and a tetrafluoroethylene unit; a non-fluorinated polymer layer (N2) containing an aliphatic polyamide resin; a non-fluorinated polymer layer (A) containing an ethylene / vinyl alcohol copolymer; a non-fluorinated polymer layer (N2) containing an aliphatic polyamide resin, and a non-fluorinated polymer layer (N2) containing an aliphatic polyamide resin; In this order, The fluororesin layer (F) is the innermost layer and comes into contact with the fuel. Tube or hose.

Images