CN116964113A - Copolymer, molded body, injection molded body, and coated electric wire - Google Patents

Copolymer, molded body, injection molded body, and coated electric wire Download PDF

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Publication number
CN116964113A
CN116964113A CN202280016007.5A CN202280016007A CN116964113A CN 116964113 A CN116964113 A CN 116964113A CN 202280016007 A CN202280016007 A CN 202280016007A CN 116964113 A CN116964113 A CN 116964113A
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copolymer
present
less
molded article
ppve
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井坂忠晴
善家佑美
山本有香里
津田早登
关口岳史
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Daikin Industries Ltd
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Daikin Industries Ltd
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Priority claimed from PCT/JP2022/003636 external-priority patent/WO2022181222A1/en
Publication of CN116964113A publication Critical patent/CN116964113A/en
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Abstract

The present invention provides a copolymer comprising tetrafluoroethylene units and perfluoro (propyl vinyl ether) units, wherein the content of the perfluoro (propyl vinyl ether) units is 2.26 to 2.75 mol% relative to the total monomer units, the melt flow rate at 372 ℃ is 4.0g/10 min to 11.0g/10 min, and the number of functional groups is per 10 6 The number of carbon atoms of the main chain is 50 or less.

Description

Copolymer, molded body, injection molded body, and coated electric wire
Technical Field
The present invention relates to a copolymer, a molded body, an injection molded body, and a coated electric wire.
Background
Patent document 1 describes a molding material for ozone-resistant articles, which is composed of a copolymer (a) having a melt flow rate of 0.1g/10 min to 50g/10 min, and is characterized in that the copolymer (a) is a copolymer composed of tetrafluoroethylene and perfluorovinyl ether, contains 3.5 mass% or more of perfluorovinyl ether units, has a melting point of 295 ℃ or more, and has unstable terminal groups per 1×10 of the copolymer (a) 6 The number of carbon atoms is 50 or less.
Prior art literature
Patent literature
Patent document 1: international publication No. 2003/048214
Disclosure of Invention
Problems to be solved by the invention
The purpose of the present invention is to provide a copolymer which can be molded by an injection molding method to give a beautiful injection molded article, which is less likely to corrode a mold or a coated core wire used in molding, which can form a very thick coating layer with a uniform thickness on a very large diameter core wire by an extrusion molding method, which can give a molded article having a very small haze value, a very excellent abrasion resistance, a mechanical strength at 100 ℃, a low permeability for carbon dioxide, a low permeability for a reagent, a high rigidity and a non-tackiness at 110 ℃, and which is less likely to be damaged or deteriorated even under repeated tensile load, and which has a sufficient low permeability for water vapor and is less likely to cause elution of fluorine ions into an electrolyte.
Means for solving the problems
According to the present invention, there is provided a copolymer comprising tetrafluoroethylene units and perfluoro (propyl ethyl)Alkenyl ether) units, the content of perfluoro (propyl vinyl ether) units relative to the total monomer units being 2.26 to 2.75 mol%, the melt flow rate at 372 ℃ being 4.0g/10 min to 11.0g/10 min, the number of functional groups being per 10 6 The number of carbon atoms of the main chain is 50 or less.
In the copolymer of the present invention, the melt flow rate at 372℃is preferably 5.0g/10 min to 10.0g/10 min.
Further, according to the present invention, there is provided an injection molded article comprising the copolymer.
Further, according to the present invention, there is provided a coated wire comprising a coating layer containing the copolymer.
Further, according to the present invention, there is provided a molded article comprising the copolymer, wherein the molded article is a filter case, a film, a bottle, a wire coating or a tube.
ADVANTAGEOUS EFFECTS OF INVENTION
According to the present invention, it is possible to provide a copolymer which can be molded by injection molding to obtain an injection molded article having a beautiful appearance, which is less likely to corrode a mold or a coated core wire used in molding, which can form a very thick coating layer with a uniform thickness on a very large diameter core wire by extrusion molding, which has a very small haze value, which is very excellent in abrasion resistance, which has a mechanical strength at 100 ℃, which has a low permeability to carbon dioxide, which has a low permeability to a reagent, which has excellent rigidity and non-tackiness at a high temperature of 110 ℃, and which is less likely to be damaged or deteriorated even under repeated tensile load, and which has a sufficient low permeability to water vapor and is less likely to cause elution of fluorine ions into an electrolyte.
Detailed Description
Hereinafter, specific embodiments of the present invention will be described in detail, but the present invention is not limited to the following embodiments.
The copolymers of the present invention contain Tetrafluoroethylene (TFE) units and perfluoro (propyl vinyl ether) (PPVE) units.
A copolymer (PFA) containing TFE units and PPVE units is used as a material for forming a filter housing used for filtering a fluid such as a reagent. The pressure of the fluid passing through the filter housing frequently fluctuates at the start of supply of the fluid, at the stop of supply of the fluid, at the time of change of the supply pressure of the fluid, and the like. When high pressure fluid or high temperature fluid is filtered, the high pressure fluid or high temperature fluid passes through the filter housing. Therefore, as a material constituting the filter case, a material excellent in durability against repeated stress and mechanical strength at high temperature is required. Meanwhile, in order to allow the defoaming operation to be performed while visually checking whether or not bubbles are present in the filter housing, it is preferable to use a material having excellent transparency for the material constituting the filter housing. In order to prevent the reagent flowing through the filter case from being contaminated with moisture, fluoride ions, and the like, it is necessary to use a material that has sufficient low permeability to water vapor, is excellent in low permeability, and suppresses elution of fluoride ions from the material itself.
Patent document 1 describes that a molding material for ozone resistant articles having the above-described characteristics is a molding material excellent in ozone resistance in a state where the chemical resistance, heat resistance and mechanical properties of a fluororesin are maintained without impairing the physical properties and moldability of the fluororesin. However, there is a need for a copolymer which has sufficient mechanical strength at high temperature, sufficient low water vapor permeability and sufficient low reagent permeability, is less likely to cause elution of fluorine ions, and is capable of providing a molded article having a small haze value and less likely to be damaged even under repeated tensile load, as compared with the molded material described in patent document 1.
Further, in order to manufacture the filter housing with high productivity, it is preferable to mold the material using an injection molding method. In the case of the conventional material, even if the transparency of the material itself is excellent, there is a problem that a filter case excellent in transparency cannot be obtained because cloudiness or roughness is observed on the surface of the obtained injection-molded article. Therefore, as a material constituting the filter housing, a material having not only a small haze value of the material itself but also excellent moldability and not impairing excellent transparency after injection molding is demanded.
The discovery is as follows: by properly adjusting the content of PPVE unit, melt Flow Rate (MFR) and the number of functional groups of the copolymer containing TFE unit and PPVE unit, the moldability of the copolymer is remarkably improved while the mold for molding is not easily corroded. It was also found that: by using such a copolymer, a molded article having a very small haze value, excellent abrasion resistance, mechanical strength at 100 ℃, low permeability to carbon dioxide, low permeability to a reagent, excellent rigidity and non-adhesive properties at a high temperature of 110 ℃, being less likely to be damaged or deteriorated even under repeated tensile load, having sufficient low permeability to steam, and being less likely to dissolve out fluorine ions into an electrolyte can be obtained.
Further, the copolymer of the present invention can form a very thick coating layer with a uniform thickness on a very large diameter core wire by extrusion molding. Further, the obtained coating layer is less likely to corrode the core wire. Thus, the copolymer of the present invention can be used not only as a material for a filter case but also for a wide range of applications such as wire coating.
The copolymer of the present invention is a melt-processible fluororesin. Melt processability means that a polymer can be melted and processed using existing processing equipment such as an extruder and an injection molding machine.
The PPVE unit content of the copolymer is 2.26 mol% to 2.75 mol%, preferably 2.28 mol% or more, more preferably 2.30 mol% or more, further preferably 2.32 mol% or more, particularly preferably 2.34 mol% or more, most preferably 2.38 mol% or more, preferably 2.71 mol% or less, more preferably 2.68 mol% or less, further preferably 2.65 mol% or less, particularly preferably 2.62 mol% or less, and most preferably 2.59 mol% or less, based on the total monomer units. When the content of the PPVE unit in the copolymer is in the above range, a molded article having a very small haze value, very excellent abrasion resistance, mechanical strength at 100 ℃, low permeability to carbon dioxide, low permeability to a reagent, excellent rigidity and non-tackiness at a high temperature of 110 ℃, little possibility of damage or deterioration even under repeated tensile load, and sufficient low permeability to water vapor can be obtained. If the content of PPVE unit in the copolymer is too small, the haze value becomes large or the abrasion resistance is poor. If the PPVE unit content of the copolymer is too large, a molded article having sufficient low permeability to water vapor, a molded article having sufficient low permeability to carbon dioxide, a molded article having sufficient rigidity at a high temperature of 110 ℃, or a molded article having excellent durability against repeated tensile load cannot be obtained.
The TFE unit content of the copolymer is preferably 97.25 mol% to 97.74 mol%, more preferably 97.29 mol% or more, still more preferably 97.32 mol% or more, still more preferably 97.35 mol% or more, particularly preferably 97.38 mol% or more, most preferably 97.41 mol% or more, more preferably 97.72 mol% or less, still more preferably 97.70 mol% or less, still more preferably 97.68 mol% or less, particularly preferably 97.66 mol% or less, and most preferably 97.62 mol% or less, based on the total monomer units. If the TFE unit content of the copolymer is too large, the haze value may be increased. If the TFE unit content of the copolymer is too small, there is a possibility that a molded article having sufficient low water vapor permeability cannot be obtained.
In the present invention, the content of each monomer unit in the copolymer is determined by 19 F-NMR measurement.
The copolymer may also contain monomer units derived from monomers copolymerizable with TFE and FAVE. In this case, the content of the monomer unit copolymerizable with TFE and PPVE is preferably 0 to 0.45 mol%, more preferably 0.01 mol% to 0.30 mol% or less, and still more preferably 0.05 mol% to 0.20 mol% based on the total monomer units of the copolymer.
Examples of monomers copolymerizable with TFE and PPVE include Hexafluoropropylene (HFP) and CZ 1 Z 2 ＝CZ 3 (CF 2 ) n Z 4 (wherein Z is 1 、Z 2 And Z 3 Identical or different, H or F, Z 4 H, F or Cl, n represents an integer of 2 to 10), and CF) 2 ＝CF-ORf 1 (wherein Rf 1 Perfluoro (alkyl vinyl ether) [ PAVE ] represented by perfluoroalkyl group having 1 to 8 carbon atoms](except PPVE), and CF 2 ＝CF-OCH 2 -Rf 1 (wherein Rf 1 Perfluoro-alkane with 1-5 carbon atomsA base. ) Alkyl perfluorovinyl ether derivatives shown and the like. Among them, HFP is preferable.
The copolymer is preferably at least one selected from the group consisting of a copolymer composed of only TFE units and PPVE units, and a TFE/HFP/PPVE copolymer, and more preferably a copolymer composed of only TFE units and PPVE units.
The Melt Flow Rate (MFR) of the copolymer is 4.0g/10 min to 11.0g/10 min. The MFR of the copolymer is preferably 4.1g/10 min or more, more preferably 4.2g/10 min or more, still more preferably 4.3g/10 min or more, still more preferably 4.5g/10 min or more, particularly preferably 5.0g/10 min or more, particularly preferably 6.0g/10 min or more, most preferably 7.0g/10 min or more, preferably 10.9g/10 min or less, still more preferably 10.5g/10 min or less, still more preferably 10.4g/10 min or less, still more preferably 10.0g/10 min or less, particularly preferably 9.5g/10 min or less, and most preferably 9.0g/10 min or less. When the MFR of the copolymer is in the above range, the moldability of the copolymer is improved, and a molded article having a small haze value, less likely to be damaged even under repeated tensile load, abrasion resistance, mechanical strength at 100 ℃, low permeability to carbon dioxide, low permeability to a reagent, excellent rigidity at 110 ℃ and sufficient low permeability to water vapor can be obtained.
In the present invention, MFR is a value obtained as a mass (g/10 min) of a polymer flowing out from a nozzle having an inner diameter of 2.1mm and a length of 8mm at 372℃under a 5kg load every 10 minutes using a melt index meter according to ASTM D1238.
The MFR can be adjusted by adjusting the kind and amount of a polymerization initiator used in polymerizing the monomers, the kind and amount of a chain transfer agent, and the like.
Every 10 of the copolymer 6 The number of functional groups having the number of main chain carbon atoms is 50 or less. Every 10 of the copolymer 6 The number of functional groups having the number of main chain carbon atoms is preferably 40 or less, more preferably 30 or less, further preferably 20 or less, still more preferably 15 or less, particularly preferably 10 or less, and most preferably less than 6. By having the number of functional groups of the copolymer within the above range, even byThe molding of the copolymer by filling the copolymer into the mold is not liable to corrode the mold, and the core wire is not liable to corrode even when used as a coating of an electric wire. Further, a molded article having excellent non-tackiness, low permeability to carbon dioxide and low permeability to a reagent, and being less likely to cause elution of fluorine ions into an electrolyte solution can be obtained. In particular, by properly adjusting the content of PPVE unit, melt Flow Rate (MFR) and the number of functional groups of the copolymer containing TFE unit and PPVE unit, a molded article exhibiting excellent low permeability to various reagents such as dimethyl carbonate and ethyl acetate can be obtained.
The identification of the kind of the functional group and the measurement of the number of functional groups may be performed by infrared spectroscopic analysis.
Specifically, the number of functional groups was measured by the following method. First, the copolymer was cold-molded to prepare a film having a thickness of 0.25mm to 0.3 mm. The film was analyzed by fourier transform infrared spectroscopy to obtain the infrared absorption spectrum of the above copolymer, and to obtain a differential spectrum from the fully fluorinated background spectrum without functional groups. The specific absorption peak of the specific functional group in the copolymer was calculated for every 1X 10 based on the following formula (A) 6 Number of functional groups N of carbon atoms.
N＝I×K/t(A)
I: absorbance of light
K: correction coefficient
t: film thickness (mm)
For reference, the absorption frequency, molar absorptivity, and correction factor are shown in table 1 for some functional groups. The molar absorptivity was determined from FT-IR measurement data of the low molecular weight model compound.
TABLE 1
TABLE 1
-CH 2 CF 2 H、-CH 2 COF、-CH 2 COOH、-CH 2 COOCH 3 、-CH 2 CONH 2 The absorption frequency ratios of (C) are shown in the tables respectively for-CF 2 H. -COF, free-COOH and bonded-COOH, -COOCH 3 、-CONH 2 The absorption frequency is tens of kesai (cm- 1 )。
For example, the functional group number of-COF means the number of functional groups derived from-CF 2 Absorption frequency of COF 1883cm- 1 The number of functional groups obtained from the absorption peak at the site and the number of functional groups obtained from the absorption peak derived from-CH 2 Absorption frequency of COF 1840cm- 1 The total number of functional groups obtained from the absorption peak at the position.
The functional groups are functional groups present at the main chain end or side chain end of the copolymer and functional groups present in the main chain or side chain. The number of functional groups may be-cf=cf 2 、-CF 2 H、-COF、-COOH、-COOCH 3 、-CONH 2 and-CH 2 Total number of OH.
The functional group is introduced into the copolymer, for example, by a chain transfer agent or a polymerization initiator used in producing the copolymer. For example, using alcohols as chain transfer agents, or using compounds having-CH 2 In the case of peroxides of OH structure as polymerization initiators, -CH 2 OH is introduced into the backbone end of the copolymer. In addition, the functional group is introduced into the terminal of the side chain of the copolymer by polymerizing a monomer having the functional group.
By subjecting the copolymer having such a functional group to fluorination treatment, a copolymer having the number of functional groups in the above range can be obtained. That is, the copolymer of the present invention is preferably a fluorinated copolymer. The copolymers of the invention also preferably have-CF 3 End groups.
The melting point of the copolymer is preferably 285 to 310 ℃, more preferably 290 ℃ or higher, still more preferably 294 ℃ or higher, particularly preferably 296 ℃ or higher, most preferably 298 ℃ or higher, and still more preferably 305 ℃ or lower. When the melting point is within the above range, a copolymer which provides a molded article having more excellent mechanical strength particularly at high temperature can be obtained.
In the present invention, the melting point can be measured using a differential scanning calorimeter [ DSC ].
The haze value of the copolymer of the present invention is preferably 7.5% or less. When the haze value is in the above range, for example, in the case of obtaining a molded article such as a pipe, a joint, a bottle, or a flowmeter using the copolymer of the present invention, the inside of the molded article can be easily observed by visual observation, a camera, or the like, and the flow rate and the remaining amount of the content can be easily confirmed. The haze value can be reduced by adjusting the PPVE unit content and Melt Flow Rate (MFR) of the copolymer. In the present invention, the haze value can be measured according to JIS K7136.
The copolymer of the present invention preferably has a tensile strength at 100℃of 20.0MPa or more, more preferably 20.5MPa or more, and still more preferably 22.0MPa or more. By setting the tensile strength at 100℃in the above range, even when the obtained molded article is used at a high temperature, deformation can be suppressed, and a longer life of the molded article can be achieved. The tensile strength at 100℃can be increased by adjusting the PPVE unit content and the Melt Flow Rate (MFR) of the copolymer. In the present invention, the tensile strength at 100℃can be measured according to ASTM D638.
The copolymer preferably has a water vapor permeability of 18.0 g.cm/m 2 Hereinafter, it is more preferably 17.5 g.cm/m 2 Hereinafter, it is more preferably 17.0 g.cm/m 2 The following is given. The copolymer of the present invention has sufficient low water vapor permeability because the content of PPVE unit, melt Flow Rate (MFR) and the number of functional groups of the copolymer containing TFE unit and PPVE unit are appropriately adjusted. For this reason, for example, molded articles such as filter cases obtained using the copolymer of the present invention can be suitably used for transporting a reagent that does not want to mix with moisture such as water vapor in the outside air.
In the present invention, the water vapor permeability can be measured at a temperature of 95℃for 30 days. Specific measurement of the water vapor permeability can be performed by the method described in examples.
The carbon dioxide permeability coefficient of the copolymer is preferably 2000cm 3 ·mm/(m 2 24 h.atm) or less. The copolymer of the present invention has a properly adjusted content of PPVE unit and melt flow rate (MFR) and the number of functional groups, and thus has excellent low permeability to carbon dioxide. Therefore, by using the copolymer of the present invention, it is possible to obtain a molded article such as a bottle which can reliably suppress permeation of carbon dioxide from the outside and can maintain the quality of the reagent stored therein for a long period of time.
In the present invention, the carbon dioxide permeability coefficient can be measured under the conditions of a test temperature of 70℃and a test humidity of 0% RH. The specific measurement of the carbon dioxide permeation coefficient can be performed by the method described in examples.
The electrolyte permeability of the copolymer is preferably 8.5 g.cm/m 2 Hereinafter, it is more preferably 8.2 g.cm/m 2 The following is given. The copolymer of the present invention has excellent electrolyte low permeability because the content of PPVE unit, melt Flow Rate (MFR) and the number of functional groups of the copolymer containing TFE unit and PPVE unit are appropriately adjusted. That is, by using the copolymer of the present invention, a molded article which is difficult to permeate a reagent such as an electrolyte can be obtained.
In the present invention, the electrolyte permeability can be measured at a temperature of 60℃for 30 days. Specific measurement of the electrolyte permeability can be performed by the method described in examples.
The copolymer preferably has an ethyl acetate permeability of 6.9 g.cm/m 2 Hereinafter, it is more preferably 6.6 g.cm/m 2 The following is given. The copolymer of the present invention has excellent ethyl acetate low permeability because the content of PPVE unit, melt Flow Rate (MFR) and the number of functional groups of the copolymer containing TFE unit and PPVE unit are appropriately adjusted. That is, by using the copolymer of the present invention, a molded article which is hard to permeate a reagent such as ethyl acetate can be obtained.
In the present invention, ethyl acetate permeability can be measured at a temperature of 60℃for 45 days. Specific measurement of ethyl acetate permeability can be performed by the method described in examples.
The amount of the eluted fluoride ion detected in the electrolyte impregnation test of the copolymer of the present invention is preferably 1.0ppm or less, more preferably 0.8ppm or less, and still more preferably 0.7ppm or less on a mass basis. By adjusting the amount of the eluted fluoride ions within the above range, the generation of gas such as HF in the nonaqueous electrolyte battery can be further suppressed, and deterioration in battery performance and short lifetime of the nonaqueous electrolyte battery can be further suppressed.
In the present invention, the electrolyte impregnation test can be performed as follows: a test piece having a weight equivalent to 10 molded articles (15 mm. Times.15 mm. Times.0.2 mm) was prepared using the copolymer, and a glass sample bottle containing the test piece and 2g of dimethyl carbonate (DMC) was placed in a constant temperature bath at 80℃for 144 hours.
The copolymer of the present invention can be produced by a polymerization method such as suspension polymerization, solution polymerization, emulsion polymerization, or bulk polymerization. As the polymerization method, emulsion polymerization or suspension polymerization is preferable. In these polymerizations, the conditions such as temperature and pressure, polymerization initiator, and other additives may be appropriately set according to the composition and amount of the copolymer.
As the polymerization initiator, an oil-soluble radical polymerization initiator or a water-soluble radical polymerization initiator can be used.
The oil-soluble radical polymerization initiator may be a known oil-soluble peroxide, and the following are exemplified as typical examples:
dialkyl peroxycarbonates such as di-n-propyl peroxydicarbonate, diisopropyl peroxydicarbonate, di-sec-butyl peroxydicarbonate, and di-2-ethoxyethyl peroxydicarbonate;
peroxyesters such as t-butyl peroxyisobutyrate and t-butyl peroxypivalate;
dialkyl peroxides such as di-t-butyl peroxide;
di [ fluoro (or fluoro chloro) acyl ] peroxides; etc.
As bis [ fluoro (or fluoro chloro) acyl groups]The peroxides include [ (RfCOO) & lt- & gt ]] 2 (Rf is perfluoroalkyl, omega-hydroperfluoroalkyl or fluorochloroalkyl).
Examples of the di [ fluoro (or fluorochloroacyl ] peroxides include di (ω -hydro-dodecafluoroheptanoyl) peroxide, di (ω -hydro-hexadecanoyl) peroxide, di (perfluoropropionyl) peroxide, di (perfluorobutanoyl) peroxide, di (perfluoropentanoyl) peroxide, di (perfluorohexanoyl) peroxide, di (perfluoroheptanoyl) peroxide, di (perfluorooctanoyl) peroxide, di (perfluorononanoyl) peroxide, di (ω -chloro-hexafluorobutanoyl) peroxide, di (ω -chloro-dodecafluoroheptanoyl) peroxide, di (ω -chloro-dodecafluorooctanoyl) peroxide, ω -hydro-dodecafluoroheptanoyl-peroxide, ω -chloro-hexafluorobutanoyl-peroxide, ω -hydrododecafluoroheptanoyl-perfluorobutanoyl-peroxide, di (perfluoroheptanoyl) peroxide, di (dichloro-heptanoyl) peroxide, di (dichloro-dodecanoyl) peroxide, and di (dichloro-dodecanoyl) dodecanoyl peroxide.
The water-soluble radical polymerization initiator may be a known water-soluble peroxide, and examples thereof include ammonium salts such as persulfuric acid, perboric acid, perchloric acid, perphosphoric acid, and percarbonic acid, potassium salts, sodium salts, disuccinic acid peroxide, and organic peroxides such as dipentaerythritol peroxide, t-butyl peroxymaleate, and t-butyl hydroperoxide. The reducing agent such as sulfite may be used in combination with the peroxide in an amount of 0.1 to 20 times the amount of the peroxide.
In the polymerization, a surfactant, a chain transfer agent and a solvent may be used, and conventionally known ones may be used, respectively.
As the surfactant, a known surfactant can be used, and for example, a nonionic surfactant, an anionic surfactant, a cationic surfactant, and the like can be used. Among them, the fluorinated anionic surfactant is preferable, and the fluorinated anionic surfactant having 4 to 20 carbon atoms, which may be linear or branched, and which may or may not contain ether-bonded oxygen (i.e., may have an oxygen atom interposed between carbon atoms), is more preferable. The amount of the surfactant to be added (relative to the polymerization water) is preferably 50ppm to 5000ppm.
Examples of the chain transfer agent include: hydrocarbons such as ethane, isopentane, n-hexane, and cyclohexane; aromatic compounds such as toluene and xylene; ketones such as acetone; acetate esters such as ethyl acetate and butyl acetate; alcohols such as methanol and ethanol; mercaptans such as methyl mercaptan; halogenated hydrocarbons such as carbon tetrachloride, chloroform, methylene chloride and methyl chloride; etc. The amount of the chain transfer agent to be added may vary depending on the amount of the chain transfer constant of the compound to be used, and is usually in the range of 0.01 to 20% by mass relative to the polymerization solvent.
Examples of the solvent include water, a mixed solvent of water and alcohol, and the like.
In the suspension polymerization, a fluorine-based solvent may be used in addition to water. As the fluorine-based solvent, CH may be mentioned 3 CClF 2 、CH 3 CCl 2 F、CF 3 CF 2 CCl 2 H、CF 2 ClCF 2 Hydrochlorofluoroalkanes such as CFHCl; CF (compact flash) 2 ClCFClCF 2 CF 3 、CF 3 CFClCFClCF 3 Isophlorofluoroalkanes; CF (compact flash) 3 CFHCFHCF 2 CF 2 CF 3 、CF 2 HCF 2 CF 2 CF 2 CF 2 H、CF 3 CF 2 CF 2 CF 2 CF 2 CF 2 CF 2 Hydrofluoroalkanes such as H; CH (CH) 3 OC 2 F 5 、CH 3 OC 3 F 5 CF 3 CF 2 CH 2 OCHF 2 、CF 3 CHFCF 2 OCH 3 、CHF 2 CF 2 OCH 2 F、(CF 3 ) 2 CHCF 2 OCH 3 、CF 3 CF 2 CH 2 OCH 2 CHF 2 、CF 3 CHFCF 2 OCH 2 CF 3 Isohydrofluoroethers; perfluorocyclobutane, CF 3 CF 2 CF 2 CF 3 、CF 3 CF 2 CF 2 CF 2 CF 3 、CF 3 CF 2 CF 2 CF 2 CF 2 CF 3 Among them, perfluoroalkanes are preferable. The amount of the fluorine-based solvent to be used is preferably 10 to 100% by mass based on the aqueous medium in view of suspension property and economy.
The polymerization temperature is not particularly limited, and may be 0 to 100 ℃. The polymerization pressure is appropriately determined depending on the kind and amount of the solvent used, the vapor pressure, the polymerization temperature, and other polymerization conditions, and may be generally 0 to 9.8MPaG.
When an aqueous dispersion containing a copolymer is obtained by polymerization, the copolymer contained in the aqueous dispersion can be precipitated, washed, and dried to recover the copolymer. In addition, in the case where the copolymer is obtained as a slurry by polymerization, the copolymer can be recovered by taking out the slurry from the reaction vessel, washing it, and drying it. The copolymer can be recovered in the form of a powder by drying.
The copolymer obtained by polymerization may be molded into pellets. The molding method for molding the pellets is not particularly limited, and conventionally known methods can be used. For example, a method of melt-extruding a copolymer using a single screw extruder, a twin screw extruder, or a tandem extruder, cutting the copolymer into a predetermined length, and molding the copolymer into pellets, and the like can be mentioned. The extrusion temperature at the time of melt extrusion is required to be changed depending on the melt viscosity of the copolymer and the production method, and is preferably from +20℃to +140℃of the melting point of the copolymer. The method of cutting the copolymer is not particularly limited, and conventionally known methods such as a wire cutting method, a thermal cutting method, an underwater cutting method, and a sheet cutting method can be employed. The volatile components in the pellets may also be removed by heating the resulting pellets (degassing treatment). The obtained pellets may be treated by contacting them with warm water at 30 to 200 ℃, steam at 100 to 200 ℃ or hot air at 40 to 200 ℃.
The copolymer obtained by polymerization may also be subjected to a fluorination treatment. The fluorination treatment may be performed by contacting the copolymer that has not been subjected to the fluorination treatment with a fluorine-containing compound. By fluorination treatment, the-COOH, -COOCH-of the copolymer can be obtained 3 、-CH 2 OH、-COF、-CF＝CF 2 、-CONH 2 Isothermally labile functional groups and relatively thermally stable-CF 2 Conversion of functional groups such as H to extremely thermally stable-CF 3 . Its knotAs a result, the-COOH, -COOCH-of the copolymer can be reduced 3 、-CH 2 OH、-COF、-CF＝CF 2 、-CONH 2 and-CF 2 The total number of H (the number of functional groups) is easily adjusted to be within the above-mentioned range.
The fluorine-containing compound is not particularly limited, and examples thereof include a fluorine radical source that generates a fluorine radical under the fluorination treatment conditions. As the fluorine radical source, F may be mentioned 2 Gas, coF 3 、AgF 2 、UF 6 、OF 2 、N 2 F 2 、CF 3 OF, fluorinated halogens (e.g. IF 5 、ClF 3 ) Etc.
F 2 The fluorine radical source such as gas may be used at a concentration of 100%, but from the viewpoint of safety, it is preferably used by mixing with an inactive gas and diluting to 5 to 50% by mass, more preferably 15 to 30% by mass. The inert gas may be nitrogen, helium, argon, or the like, and nitrogen is preferable from the viewpoint of economy.
The conditions of the fluorination treatment are not particularly limited, and the copolymer in a molten state may be brought into contact with the fluorine-containing compound, but may be usually conducted at a temperature of 20 to 240℃and more preferably 100 to 220℃below the melting point of the copolymer. The fluorination treatment is generally carried out for 1 to 30 hours, preferably 5 to 25 hours. The fluorination treatment preferably involves reacting the copolymer which has not been subjected to the fluorination treatment with fluorine gas (F 2 Gas) contact.
The copolymer of the present invention may be mixed with other components as needed to obtain a composition. Examples of the other components include fillers, plasticizers, processing aids, mold release agents, pigments, flame retardants, lubricants, light stabilizers, weather stabilizers, conductive agents, antistatic agents, ultraviolet absorbers, antioxidants, foaming agents, perfumes, oils, softeners, dehydrofluorination agents, and the like.
Examples of the filler include silica, kaolin, clay, organized clay, talc, mica, alumina, calcium carbonate, calcium terephthalate, titanium oxide, calcium phosphate, calcium fluoride, lithium fluoride, crosslinked polystyrene, potassium titanate, carbon, boron nitride, carbon nanotubes, and glass fibers. Examples of the conductive agent include carbon black. Examples of the plasticizer include dioctyl phthalate and pentaerythritol. Examples of the processing aid include carnauba wax, sulfone compound, low molecular weight polyethylene, and fluorine-based aid. Examples of the dehydrofluorination agent include organic onium and amidines.
As the other components, other polymers than the above copolymers may be used. Examples of the other polymer include a fluororesin other than the above copolymer, a fluororubber, a nonfluorinated polymer, and the like.
The method for producing the composition includes: a method of dry-mixing the copolymer with other components; a method in which the copolymer and other components are mixed in advance by a mixer, and then melt-kneaded by a kneader, a melt extruder, or the like; etc.
The copolymer or the composition of the present invention can be used as a processing aid, a molding material, or the like, and is preferably used as a molding material. Aqueous dispersions, solutions, suspensions, and copolymer/solvent systems of the copolymers of the present invention may also be utilized, which may be applied as coatings or used for encapsulation, impregnation, film casting. However, the copolymer of the present invention is preferably used as the molding material because it has the above-mentioned characteristics.
The copolymer of the present invention or the above composition may be molded to obtain a molded article.
The method for molding the copolymer or the composition is not particularly limited, and examples thereof include injection molding, extrusion molding, compression molding, blow molding, transfer molding, rotational molding, and roll lining molding. Among the molding methods, extrusion molding, compression molding, injection molding or transfer molding is preferable, and injection molding is more preferable because a molded article can be produced with high productivity. That is, the molded article is preferably an extrusion molded article, a compression molded article, an injection molded article or a transfer molded article, and more preferably an injection molded article, an extrusion molded article or a transfer molded article, and even more preferably an injection molded article, since it can be produced at high productivity. By molding the copolymer of the present invention by injection molding, an injection molded article having a beautiful appearance can be obtained without corroding a mold for molding.
Examples of molded articles containing the copolymer of the present invention include nuts, bolts, joints, films, bottles, gaskets, wire coatings, pipes, hoses, pipes, valves, sheets, seals, gaskets, tanks, rolls, containers, taps, connectors, filter housings, filter covers, flow meters, pumps, wafer carriers, wafer cassettes, and the like.
The copolymer, the composition or the molded article of the present invention can be used for the following purposes, for example.
A film for packaging food, a lining material for a fluid transfer line used in a food manufacturing process, a gasket, a sealing material, a fluid transfer member for a food manufacturing apparatus such as a sheet;
reagent delivery members such as plugs for chemicals, packaging films, liners for fluid delivery lines used in chemical manufacturing processes, gaskets, seals, sheets, etc.;
inner lining members of reagent tanks and piping of chemical equipment and semiconductor factories;
fuel delivery members such as hoses and sealing materials used in AT devices of automobiles such as O (square) rings/tubes/gaskets, valve core materials, hoses and sealing materials used in fuel systems and peripheral devices of automobiles;
flange gaskets, shaft seals, stem seals, sealing materials, brake hoses for automobiles such as hoses, air conditioning hoses, radiator hoses, wire coating materials, and other automobile components used in engines and peripheral devices of automobiles;
A reagent transporting member for a semiconductor device, such as an O-ring, a tube, a gasket, a valve body material, a hose, a sealing material, a roller, a gasket, a diaphragm, and a joint of a semiconductor manufacturing apparatus;
coating and ink members such as coating rolls, hoses, tubes, ink containers for coating equipment;
pipes such as pipes for food and drink, hoses, belts, gaskets, joints, and other food and drink conveying members, food packaging materials, and glass cooking devices;
a waste liquid transporting member such as a tube or a hose for transporting waste liquid;
high-temperature liquid transmission members such as pipes and hoses for high-temperature liquid transmission;
a member for steam piping such as a pipe or a hose for steam piping;
a corrosion-resistant belt for piping such as a belt wound around piping such as a deck of a ship;
various coating materials such as a wire coating material, an optical fiber coating material, a transparent surface coating material provided on a light incidence side surface of a photovoltaic element of a solar cell, and a back surface agent;
sliding components such as diaphragms and various gaskets of the diaphragm pump;
weather resistant covers for agricultural films, various roofing materials, sidewalls, and the like;
glass-like coating materials such as interior materials and incombustible fire-resistant safety glass used in the construction field;
Lining materials such as laminated steel sheets used in the field of home appliances and the like.
Further examples of the fuel delivery member used in the fuel system of the automobile include a fuel hose, a filler hose, and an evaporator hose. The fuel delivery member can be used as a fuel delivery member for acid-resistant gasoline, alcohol-resistant fuel, and fuel to which a gasoline additive such as methyl t-butyl ether or amine-resistant additive is added.
The above-mentioned chemical stopper and packaging film have excellent chemical resistance to acids and the like. The reagent transporting member may be an anti-corrosive tape wound around a piping of a chemical apparatus.
Examples of the molded article include radiator chambers, reagent tanks, bellows, separators, rolls, gasoline tanks, waste liquid transport containers, high-temperature liquid transport containers, fishery and fish farming tanks, and the like of automobiles.
Further, examples of the molded article include a bumper, a door trim, an instrument panel, a food processing device, a cooking machine, water/oil resistant glass, a lighting-related instrument, an indication board and a housing for OA instruments, an electric lighting sign, a display screen, a liquid crystal display, a cellular phone, a printer chassis, electric and electronic parts, sundries, a dustbin, a bathtub, an entire bathroom, a ventilator, a lighting frame, and the like.
The molded article containing the copolymer of the present invention has extremely small haze value, extremely excellent abrasion resistance, excellent mechanical strength at 100 ℃, low permeability to carbon dioxide, low permeability to a reagent, excellent rigidity and non-tackiness at a high temperature of 110 ℃, and is not easily damaged or deteriorated even under repeated tensile load, and has sufficient low permeability to water vapor, and is not easily eluted fluorine ions into an electrolyte, and therefore can be suitably used for nuts, bolts, joints, gaskets, valves, taps, connectors, filter housings, filter housing, flow meters, pumps, and the like. The filter housing containing the copolymer of the present invention has a very small haze value, and thus is excellent in visibility of the inside, and for example, can be easily subjected to a defoaming operation. The present invention can be suitably used as a piping member (particularly, a joint) for transporting a reagent or a flowmeter body having a flow path for a reagent in a flowmeter. The piping member and the flowmeter body of the present invention have extremely small haze values, extremely excellent abrasion resistance, excellent mechanical strength at 100 ℃, low permeability to carbon dioxide, low permeability to a reagent, excellent rigidity and non-adhesion at a high temperature of 110 ℃, and are less likely to be damaged or deteriorated even under repeated tensile load, have sufficient low permeability to water vapor, and are less likely to dissolve out fluoride ions into an electrolyte. Therefore, the piping member and the flowmeter body of the present invention are excellent in visibility, and particularly in the flowmeter body, the float in the flowmeter body can be easily observed by visual observation, a camera, or the like, and the piping member and the flowmeter body can be suitably used for measuring the flow rate of a reagent at about 100 ℃, and are less likely to be damaged even if stress is repeatedly applied according to the start of the flow of the reagent, the stop of the flow, and the change of the flow rate. Further, the piping member and the flowmeter body of the present invention can be manufactured by injection molding without corroding a mold for molding, and have a beautiful appearance.
The molded article containing the copolymer of the present invention can be easily produced by injection molding without corroding a mold, has a very small haze value, is excellent in abrasion resistance, is excellent in mechanical strength at 100 ℃, low in permeability to carbon dioxide, low in permeability to a reagent, is excellent in rigidity and non-adhesiveness at a high temperature of 110 ℃, is not easily damaged or deteriorated even under repeated tensile load, has sufficient low permeability to water vapor, and is not easily eluted with fluorine ions into an electrolyte, and therefore can be suitably used as a compressed member such as a gasket or a gasket. The compressed member of the present invention may be a gasket or a seal. The gasket or the gasket of the present invention can be manufactured at low cost by injection molding without corroding a mold, is less likely to be damaged even when provided at a site that is repeatedly opened and closed at a high frequency, and has excellent mechanical strength at 100 ℃. The compressed member of the present invention is excellent in low water vapor permeability and is not easily damaged even by repeated load stress, and therefore can be suitably used as a piping member for transporting a reagent which is not intended to be mixed with moisture such as water vapor in an external atmosphere.
The size and shape of the compressed member of the present invention may be appropriately set according to the application, and are not particularly limited. The compressed member of the present invention may be annular in shape, for example. The compressed member of the present invention may have a circular shape, an elliptical shape, a quadrangular shape with rounded corners, or the like in a plan view, and may have a through hole in a central portion thereof.
The compressed member of the present invention is preferably used as a member for constituting a nonaqueous electrolyte battery. The compressed member of the present invention is excellent in low water vapor permeability and is not likely to cause elution of fluorine ions into an electrolyte, and therefore is particularly suitable as a member used in a state of contact with a nonaqueous electrolyte in a nonaqueous electrolyte battery. That is, the compressed member of the present invention may have a liquid receiving surface of the nonaqueous electrolyte in the nonaqueous electrolyte battery.
The compressed member of the present invention is less likely to cause elution of fluorine ions into a nonaqueous electrolytic solution. Therefore, by using the compressed member of the present invention, an increase in the fluoride ion concentration in the nonaqueous electrolytic solution can be suppressed. As a result, by using the compressed member of the present invention, the generation of gas such as HF in the nonaqueous electrolyte battery can be suppressed, or the deterioration of the battery performance and the reduction of the lifetime of the nonaqueous electrolyte battery can be suppressed.
The compressed member of the present invention can further suppress the generation of gas such as HF in the nonaqueous electrolyte battery or can further suppress the deterioration of battery performance and the reduction of lifetime of the nonaqueous electrolyte battery, and therefore the amount of dissolved fluorine ions detected in the electrolyte impregnation test is preferably 1.0ppm or less, preferably 0.8ppm or less, more preferably 0.7ppm or less on a mass basis. The electrolyte impregnation test can be performed as follows: a test piece having a weight equivalent to 10 molded articles (15 mm. Times.15 mm. Times.0.2 mm) was produced using the compressed member, and a glass sample bottle containing the test piece and 2g of dimethyl carbonate (DMC) was placed in a constant temperature bath at 80℃for 144 hours.
The compressed member of the present invention is not easily permeable to water vapor. Therefore, by using the compressed member of the present invention, the permeation of water vapor from the outside through the secondary battery can be suppressed. As a result, by using the compressed member of the present invention, deterioration in battery performance and short lifetime of the nonaqueous electrolyte battery can be suppressed.
The compressed member of the present invention preferably has a water vapor permeability of 18.0 g/cm/m because deterioration in battery performance and short lifetime of the nonaqueous electrolyte battery can be further suppressed 2 Hereinafter, it is more preferably 17.5 g.cm/m 2 Hereinafter, it is more preferably 17.0 g.cm/m 2 The following is given. The water vapor permeability of the compressed member can be measured at a temperature of 95℃for 30 days.
The nonaqueous electrolyte battery is not particularly limited as long as it is a battery provided with a nonaqueous electrolyte, and examples thereof include a lithium ion secondary battery and a lithium ion capacitor. Further, as a member constituting the nonaqueous electrolyte battery, a sealing member, an insulating member, and the like can be given.
The nonaqueous electrolyte is not particularly limited, and propylene carbonate, ethylene carbonate, butylene carbonate, gamma-butyrolactone, 1, 2-dimethoxyethane may be used1 or 2 or more of known solvents such as 1, 2-diethoxyethane, dimethyl carbonate, diethyl carbonate and methylethyl carbonate. The nonaqueous electrolyte battery may further include an electrolyte. The electrolyte is not particularly limited, and LiClO may be used 4 、LiAsF 6 、LiPF 6 、LiBF 4 、LiCl、LiBr、CH 3 SO 3 Li、CF 3 SO 3 Li, cesium carbonate, and the like.
The compressed member of the present invention can be preferably used as a sealing member such as a gasket or a packing, or an insulating member such as an insulating gasket or an insulating packing, for example. The sealing member is used to prevent leakage of liquid or gas or intrusion of liquid or gas from the outside. The insulating member is a member used for electrical insulation. The compressed member of the present invention may be a member used for both sealing and insulation purposes.
The compressed member of the present invention is not likely to cause elution of fluorine ions into an electrolyte solution, and therefore can be suitably used as a sealing member for a nonaqueous electrolyte battery or an insulating member for a nonaqueous electrolyte battery. In addition, the compressed member of the present invention has excellent insulating properties because it contains the copolymer. Therefore, when the compressed member of the present invention is used as an insulating member, the compressed member is firmly adhered to 2 or more conductive members, and short-circuiting can be prevented for a long period of time.
The copolymer of the present invention is less likely to corrode the coated core wire. Further, by molding the copolymer of the present invention by extrusion molding, a very thick coating layer can be formed with a uniform thickness on a core wire having a very large diameter, and thus can be suitably used as a material for forming an electric wire coating. Therefore, the core wire of the coated wire having the coating layer containing the copolymer of the present invention is less likely to corrode, and the outer diameter is hardly changed, so that the electric characteristics are excellent.
When a very thick coating layer is formed on a very large diameter core wire with a uniform thickness, it takes a long time until the coating layer in a molten state is solidified, and the weight of the coating layer is also large, so that when a conventional copolymer is used, the coating layer is deformed by its own weight before solidification, and there is a problem that it is difficult to form a coating layer with a uniform thickness. By using the copolymer of the present invention, a very thick coating layer can be formed with a uniform thickness.
The coated wire comprises a core wire and a coating layer provided around the core wire and containing the copolymer of the present invention. For example, an extrusion molded article obtained by melt-extruding the copolymer of the present invention on a core wire may be used as the coating layer. The covered wire is suitable for LAN cables (Ethernet cables), high-frequency transmission cables, flat cables, heat-resistant cables, and the like, and is suitable for transmission cables such as LAN cables (Ethernet cables), high-frequency transmission cables, and the like.
As the material of the core wire, for example, a metal conductor material such as copper or aluminum can be used. The core wire preferably has a diameter of 0.02mm to 3mm. The diameter of the core wire is more preferably 0.04mm or more, still more preferably 0.05mm or more, and particularly preferably 0.1mm or more. The diameter of the core wire is more preferably 2mm or less.
Specific examples of the core wire include AWG (American wire gauge) -46 (solid copper wire with a diameter of 40 μm), AWG-26 (solid copper wire with a diameter of 404 μm), AWG-24 (solid copper wire with a diameter of 510 μm), AWG-22 (solid copper wire with a diameter of 635 μm), and the like.
The thickness of the coating layer is preferably 0.1mm to 3.0mm. The thickness of the coating layer is also preferably 2.0mm or less.
As the high-frequency transmission cable, a coaxial cable may be mentioned. The coaxial cable generally has a structure in which an inner conductor, an insulating coating layer, an outer conductor layer, and a protective coating layer are laminated in this order from a core portion to an outer peripheral portion. The molded article containing the copolymer of the present invention can be suitably used as an insulating coating layer containing the copolymer. The thickness of each layer in the above-described structure is not particularly limited, and in general, the diameter of the inner conductor is about 0.1mm to 3mm, the thickness of the insulating coating layer is about 0.3mm to 3mm, the thickness of the outer conductor layer is about 0.5mm to 10mm, and the thickness of the protective coating layer is about 0.5mm to 2mm.
The coating may contain bubbles, which are preferably uniformly distributed in the coating.
The average cell diameter of the bubbles is not limited, and is, for example, preferably 60 μm or less, more preferably 45 μm or less, further preferably 35 μm or less, further preferably 30 μm or less, particularly preferably 25 μm or less, and particularly preferably 23 μm or less. The average cell diameter is preferably 0.1 μm or more, more preferably 1 μm or more. The average bubble diameter can be obtained by obtaining an electron microscope image of a wire cross section, calculating the diameter of each bubble by image processing, and averaging.
The foaming ratio of the coating layer may be 20% or more. More preferably 30% or more, still more preferably 33% or more, still more preferably 35% or more. The upper limit is not particularly limited, and is, for example, 80%. The upper limit of the foaming ratio may be 60%. The foaming ratio was obtained as ((specific gravity of wire coating material-specific gravity of coating layer)/specific gravity of wire coating material) ×100. The foaming ratio can be appropriately adjusted according to the application by, for example, adjusting the amount of gas inserted into an extruder to be described later, or by selecting the type of dissolved gas.
The coated wire may further include a different layer (outer layer) around the coating layer, and a different layer may be provided between the core wire and the coating layer. When the coating layer contains bubbles, the electric wire of the present invention may have a 2-layer structure (skin-foam) in which a non-foam layer is interposed between the core wire and the coating layer; a 2-layer structure (foam-skin) having a non-foam layer coated on the outer layer; further, the outer layer of the skin-foam was covered with a 3-layer structure (skin-foam-skin) of a non-foam layer. The non-expanded layer is not particularly limited, and may be a resin layer composed of a polyolefin resin such as TFE/HFP copolymer, TFE/PAVE copolymer, TFE/ethylene copolymer, vinylidene fluoride polymer, polyethylene [ PE ], or a resin such as polyvinyl chloride [ PVC ].
The coated wire can be produced, for example, by heating the copolymer using an extruder, extruding the copolymer onto the core wire in a molten state, and forming a coating layer.
In forming the coating layer, the gas may be introduced into the copolymer in a molten state by heating the copolymer, thereby forming the coating layer containing bubbles. As the gas, for example, a gas such as difluoromethane, nitrogen, carbon dioxide, or the like, or a mixture of the above gases can be used. The gas may be introduced into the heated copolymer as a pressurized gas or may be produced by mixing a chemical blowing agent into the copolymer. The gas is dissolved in the copolymer in a molten state.
In addition, the copolymer of the present invention can be suitably used as a material for a product for high-frequency signal transmission.
The product for transmitting a high-frequency signal is not particularly limited as long as it is a product for transmitting a high-frequency signal, and examples thereof include (1) a molded plate such as an insulating plate for a high-frequency circuit, an insulating material for a connecting member, and a printed wiring board, (2) a molded body such as a base or a radome for a high-frequency vacuum tube, and (3) a covered wire such as a coaxial cable or a LAN cable. The high-frequency signal transmission product can be suitably used for satellite communication equipment, mobile telephone base stations, and other equipment utilizing microwaves, particularly microwaves of 3GHz to 30 GHz.
In the above-mentioned high-frequency signal transmission product, the copolymer of the present invention is suitable for use as an insulator in view of low dielectric loss tangent.
The molded plate (1) is preferably a printed wiring board in terms of obtaining good electrical characteristics. The printed wiring board is not particularly limited, and examples thereof include printed wiring boards for electronic circuits of mobile phones, various computers, communication devices, and the like. As the molded article (2), a radome is preferable in terms of low dielectric loss.
The copolymer of the present invention can be molded by injection molding to obtain a beautiful sheet. The molded article containing the copolymer of the present invention has extremely small haze value, extremely excellent abrasion resistance, excellent mechanical strength at 100 ℃, low permeability to carbon dioxide, low permeability to a reagent, excellent rigidity and non-adhesive properties at a high temperature of 110 ℃, and is not easily damaged or deteriorated even under repeated tensile load, has sufficient low permeability to steam, and is not easily eluted with fluoride ions into an electrolyte. Therefore, the molded article containing the copolymer of the present invention can be suitably used as a film or sheet.
The films of the present invention are particularly excellent in non-adhesion. Therefore, even when the film of the present invention, the resin such as epoxy resin, toner, and the like are hot-pressed, the two are not adhered, and the resin, toner, and the like can be peeled from the film.
The film of the present invention is useful as a release film. The release film can be produced by molding the copolymer of the present invention by melt extrusion molding, calender molding, press molding, casting molding, or the like. From the viewpoint of obtaining a uniform film, a release film can be produced by melt extrusion molding.
The film of the present invention can be applied to the surface of a roll used in an OA apparatus. The copolymer of the present invention can be molded into a desired shape by extrusion molding, compression molding, press molding, etc., and formed into a sheet, film, tube shape, etc., for use as a surface material for OA equipment rolls, OA equipment belts, etc. In particular, thin-walled tubes and films can be produced by melt extrusion.
The molded article containing the copolymer of the present invention has extremely small haze value, extremely excellent abrasion resistance, excellent mechanical strength at 100 ℃, low permeability to carbon dioxide, low permeability to a reagent, excellent rigidity and non-adhesive properties at a high temperature of 110 ℃, and is not easily damaged or deteriorated even under repeated tensile load, and has sufficient low permeability to water vapor and is not easily eluted fluorine ions into an electrolyte, and thus can be suitably used as a bottle or a tube. The bottle or tube of the present invention can easily visually confirm the content, and is not easily damaged in use.
While the embodiments have been described above, it will be understood that various changes in form and details may be made therein without departing from the spirit and scope of the claims.
Examples
Next, embodiments of the present invention will be described with reference to examples, but the present invention is not limited to the examples.
The values of the examples were measured by the following methods.
(content of monomer units)
The content of each monomer unit was measured by an NMR analyzer (for example, AVANCE300 high temperature probe manufactured by Bruker Biospin Co.).
(melt flow Rate (MFR))
The mass (G/10 minutes) of the polymer flowing out from a nozzle having an inner diameter of 2.1mm and a length of 8mm per 10 minutes was determined by using a melt index analyzer G-01 (manufactured by Toyo Seisakusho-Sho Co., ltd.) at 372℃under a 5kg load in accordance with ASTM D1238.
(number of functional groups)
The pellets of the copolymer were cold-molded to prepare a film having a thickness of 0.25mm to 0.3 mm. By Fourier transform infrared Spectrum analysis device [ FT-IR (Spectrum One manufactured by Perkinelmer Co.)]The film was scanned 40 times and analyzed to obtain an infrared absorption spectrum and a differential spectrum from a fully fluorinated background spectrum without functional groups. The absorbance peak of the specific functional group shown by the differential spectrum was calculated for every 1X 10 in the sample according to the following formula (A) 6 Number of functional groups N of carbon atoms.
N＝I×K/t (A)
I: absorbance of light
K: correction coefficient
t: film thickness (mm)
For reference, regarding the functional groups in the present invention, the absorption frequency, molar absorptivity, and correction coefficient are shown in table 2. The molar absorptivity was determined from FT-IR measurement data of the low molecular weight model compound.
TABLE 2
TABLE 2
(melting point)
The melting point was determined from the melting curve peak generated during the 2 nd heating process by performing the 1 st heating from 200℃to 350℃at a heating rate of 10℃per minute using a differential scanning calorimeter (trade name: X-DSC7000, manufactured by Hitachi High-Tech Science Co., ltd.), then cooling from 350℃to 200℃at a cooling rate of 10℃per minute, and performing the 2 nd heating from 200℃to 350℃again at a heating rate of 10℃per minute.
Example 1
After adding 26.6L of pure water to a 174L-volume autoclave and sufficiently performing nitrogen substitution, 30.4kg of perfluorocyclobutane, 1.96kg of perfluoro (propyl vinyl ether) (PPVE) and 0.11kg of methanol were added, the temperature in the system was kept at 35℃and the stirring speed was kept at 200rpm. Subsequently, tetrafluoroethylene (TFE) was introduced under pressure to 0.58MPa, and then 0.010kg of a 50% methanol solution of di-n-propyl peroxydicarbonate was introduced to start polymerization. Since the pressure in the system decreased as polymerization proceeded, TFE was continuously fed so that the pressure became constant, and 0.064kg of PPVE was added per 1kg of TFE fed, and polymerization was continued for 7 hours. TFE was discharged, and after the autoclave was allowed to return to atmospheric pressure, the obtained reaction product was washed with water and dried to obtain 15kg of powder.
The obtained powder was melt-extruded at 360℃by a screw extruder (trade name: PCM46, manufactured by Mitsui Co., ltd.) to obtain pellets of TFE/PPVE copolymer. Using the pellets obtained, the PPVE content was determined by the method described above. The results are shown in Table 3.
The obtained pellets were placed in a vacuum vibration type reaction apparatus VVD-30 (manufactured by Dachuan origin Co., ltd.) and heated to 210 ℃. After evacuation, N for introduction 2 F gas dilution to 20 vol% 2 The gas is brought to atmospheric pressure. From F 2 After 0.5 hour from the time of gas introduction, the mixture was once evacuated and F was introduced again 2 And (3) gas. After 0.5 hour, the mixture was again evacuated and F was introduced again 2 And (3) gas. Thereafter, F is as described above 2 The gas introduction and evacuation operations were continued for 1 time within 1 hour, and the reaction was carried out at 210℃for 10 hours. After the reaction, the inside of the reactor was fully replaced with N 2 And (3) ending the fluorination reaction by using the gas. Using the fluorinated pellets, various physical properties were measured by the above-described method. The results are shown in Table 3.
Example 2
Fluorinated pellets were obtained in the same manner as in example 1 except that PPVE was changed to 2.04kg, methanol was changed to 0.15kg, PPVE was changed to 0.066kg added per 1kg of TFE supplied, the temperature of the vacuum vibration reactor was changed to 170 ℃, and the reaction was changed to 5 hours at a temperature of 170 ℃. The results are shown in Table 3.
Example 3
Fluorinated pellets were obtained in the same manner as in example 1, except that PPVE was changed to 2.12kg, methanol was changed to 0.18kg, PPVE was changed to 0.068kg added per 1kg of TFE supplied, and the polymerization time was changed to 7.5 hours. The results are shown in Table 3.
Example 4
Fluorinated pellets were obtained in the same manner as in example 1, except that PPVE was changed to 2.20kg, methanol was changed to 0.21kg, PPVE was changed to 0.071kg per 1kg of TFE supplied, and the polymerization time was changed to 7.5 hours. The results are shown in Table 3.
Example 5
Fluorinated pellets were obtained in the same manner as in example 1, except that PPVE was changed to 2.20kg, methanol was changed to 0.23kg, PPVE was changed to 0.071kg per 1kg of TFE supplied, and the polymerization time was changed to 7.5 hours. The results are shown in Table 3.
Comparative example 1
Fluorinated pellets were obtained in the same manner as in example 1, except that PPVE was changed to 1.76kg, methanol was changed to 0.21kg, and PPVE was changed to 0.058kg added per 1kg of TFE supplied. The results are shown in Table 3.
Comparative example 2
After adding 49.0L of pure water to a 174L-volume autoclave and sufficiently replacing the pure water with nitrogen, 40.7kg of perfluorocyclobutane, 2.58kg of perfluoro (propyl vinyl ether) (PPVE) and 1.75kg of methanol were added, the temperature in the system was kept at 35℃and the stirring speed was kept at 200rpm. Subsequently, tetrafluoroethylene (TFE) was introduced under pressure to 0.64MPa, and then 0.041kg of a 50% methanol solution of di-n-propyl peroxydicarbonate was introduced to start polymerization. Since the pressure in the system decreased as polymerization proceeded, TFE was continuously fed so that the pressure became constant, and 0.071kg of PPVE was additionally fed per 1kg of TFE fed, and polymerization was continued for 18.5 hours. TFE was discharged, and after the autoclave was allowed to return to atmospheric pressure, the obtained reaction product was washed with water and dried to obtain 30kg of powder.
The obtained powder was melt-extruded at 360℃by a screw extruder (trade name: PCM46, manufactured by Mitsui Co., ltd.) to obtain pellets of TFE/PPVE copolymer. Using the pellets obtained, the PPVE content was determined by the method described above. The results are shown in Table 3.
The obtained pellets were fluorinated in the same manner as in example 1 to obtain fluorinated pellets. Using the fluorinated pellets, various physical properties were measured by the above-described method. The results are shown in Table 3.
Comparative example 3
Fluorinated pellets were obtained in the same manner as in comparative example 1, except that PPVE was changed to 2.12kg, methanol was changed to 0.03kg, PPVE was changed to 0.068kg added per 1kg of TFE supplied, and the polymerization time was changed to 7 hours. The results are shown in Table 3.
Comparative example 4
An unfluorinated pellet was obtained in the same manner as in example 1, except that the amount of methanol was changed to 0.14 kg. The results are shown in Table 3.
Comparative example 5
After filling a 174L autoclave with 51.8L of pure water and sufficiently replacing nitrogen, 40.9kg of perfluorocyclobutane, 2.88kg of perfluoro (propyl vinyl ether) (PPVE) and 1.56kg of methanol were introduced, the temperature in the system was kept at 35℃and the stirring speed was kept at 200rpm. Subsequently, tetrafluoroethylene (TFE) was introduced under pressure to 0.64MPa, and then 0.051kg of a 50% methanol solution of di-n-propyl peroxydicarbonate was introduced to start polymerization. Since the pressure in the system decreases as polymerization proceeds, TFE was continuously fed so that the pressure became constant, and 0.060kg of PPVE was additionally fed per 1kg of TFE fed. When the additional amount of TFE fed reached 40.9kg, polymerization was terminated. Unreacted TFE was discharged, and after the autoclave was allowed to return to atmospheric pressure, the obtained reaction product was washed with water and dried to obtain 41.0kg of powder.
Using the obtained powder, a fluorination reaction was performed in the same manner as in example 1 to obtain fluorinated pellets. The results are shown in Table 3.
TABLE 3
TABLE 3 Table 3
The expression "< 6" in Table 3 means that the number of functional groups is less than 6.
Next, using the obtained pellets, the following characteristics were evaluated. The results are shown in Table 4.
(haze value)
Sheets having a thickness of about 1.0mm were produced using pellets and a hot press molding machine. The sheet was immersed in a quartz dish containing pure water according to JIS K7136 using a haze meter (trade name: NDH7000SP, manufactured by Nippon Denshoku Kogyo Co., ltd.) to measure the haze value.
(tensile Strength at 100 ℃ C. (TS))
Tensile strength at 100℃was measured according to ASTM D638.
(vapor permeability)
A sheet-like test piece having a thickness of about 0.2mm was produced using the pellets and a hot press molding machine. In a test cup (permeation area 12.56 cm) 2 ) The inside was filled with 18g of water, covered with a sheet-like test piece, and fastened and sealed with a PTFE gasket interposed therebetween. The sheet-like test piece was brought into contact with water, kept at a temperature of 95℃for 30 days, taken out, left at room temperature for 2 hours, and then the mass reduction was measured. The water vapor permeability (g.cm/m) was measured by the following formula 2 )。
Water vapor permeability (g.cm/m) 2 ) =mass reduction amount (g) ×thickness (cm)/transmission area (m) of sheet-like test piece 2 )
(injection moldability)
The copolymer was injection molded using an injection molding machine (manufactured by Sumitomo mechanical industries Co., ltd., SE50 EV-A) at Sup>A cylinder temperature of 395 ℃, sup>A mold temperature of 220 ℃ and an injection speed of 3 mm/s. As the mold, a mold (100 mm×100mm×3mmt, film gate, flow length 100 mm) in which Cr plating was performed on HPM38 was used. The obtained injection-molded article was observed and evaluated according to the following criteria. The presence or absence of cloudiness was visually confirmed. The presence or absence of surface roughness was confirmed by contacting the surface of the injection-molded article.
3: the injection-molded body is transparent as a whole and has a smooth surface as a whole.
2: cloudiness was observed within 1cm from the position of the gate of the mold, and the surface was entirely smooth.
1: cloudiness was observed in a range of 1cm from the position of the gate of the mold, and roughness was confirmed on the surface in a range of 1cm from the position of the gate of the mold.
0: the entire mold is not filled with the copolymer, and a molded article having a desired shape cannot be obtained.
(electrolyte impregnation test)
About 5g of pellets were put into a mold (inner diameter: 120mm, height: 38 mm), melted at 370℃for 20 minutes by a hot plate press, and then water-cooled while being pressurized by a pressure of 1MPa (resin pressure), to prepare a molded article having a thickness of about 0.2 mm. Thereafter, using the obtained molded article, a 15mm square test piece was produced.
To a 20mL glass sample bottle, 10 pieces of the obtained test piece and 2g of dimethyl carbonate (DMC) were added, and the cap of the sample bottle was closed. The sample bottles were placed in a constant temperature bath at 80℃for 144 hours, whereby the test pieces were immersed in DMC. Then, the sample bottle was taken out of the incubator, cooled to room temperature, and then the test piece was taken out of the sample bottle. DMC remaining after the test piece was taken out was air-dried in a room at 25℃for 24 hours in a state of being placed in a sample bottle, and 2g of ultrapure water was added. The resulting aqueous solution was transferred to a cell of an ion chromatography system, and the fluorine ion content of the aqueous solution was measured by the ion chromatography system (Dionex ICS-2100, manufactured by Thermo Fisher Scientific Co.).
(ethyl acetate permeability)
A sheet-like test piece having a thickness of about 0.1mm was produced using the pellets and a hot press molding machine. In a test cup (permeation area 12.56 cm) 2 ) 10g of ethyl acetate was added thereto, and the mixture was covered with a sheet-like test piece, and fastened and sealed with a PTFE gasket interposed therebetween. The sheet-like test piece was brought into contact with ethyl acetate, kept at a temperature of 60℃for 45 days, taken out, left at room temperature for 1 hour, and then the mass reduction was measured. The ethyl acetate permeability (g.cm/m) was determined by 2 )。
Ethyl acetate (g.cm/m) 2 ) =mass reduction amount (g) ×thickness (cm)/transmission area (m) of sheet-like test piece 2 )
(110 ℃ C. Load deflection rate)
Using the pellets and a hot press molding machine, a sheet-like test piece having a thickness of about 4.2mm was produced, from which a test piece having a thickness of 80X 10mm was cut, and heated at 100℃for 20 hours by an electric furnace. The test was carried out using a thermal deformation tester (manufactured by An Tian refiner) according to the method described in JIS K-K7191, except for the test piece obtained, under conditions of a test temperature of 30 to 150 ℃, a temperature rising rate of 120 ℃/hr, a bending stress of 1.8MPa, and a flat-bed (flat-bed) method. The load deflection was obtained by the following method. The sheet having a small flexural modulus under load at 110 ℃ has excellent rigidity at a high temperature of 110 ℃.
Load deflection (%) =a2/a1×100
a1: thickness of test piece before test (mm)
a2: deflection (mm) at 110 DEG C
(tensile Strength after 10 ten thousand cycles)
The tensile strength after 10 ten-thousand cycles was measured by using a fatigue tester MMT-250NV-10 manufactured by Shimadzu corporation. A sheet having a thickness of about 2.4mm was produced using a pellet and a hot press molding machine, and a sample having a dumbbell shape (thickness: 2.4mm, width: 5.0mm, measuring section length: 22 mm) was produced using an ASTM D1708 micro dumbbell. The sample was mounted on a measurement jig, and the measurement jig was set in a constant temperature bath at 150 ℃. The uniaxial stretching was repeated at a stroke of 0.2mm and a frequency of 100Hz, and the tensile strength (tensile strength at +0.2mm in stroke, tensile strength after 10 ten thousand cycles was calculated from the measured values according to the following formula) was measured, and in this example, the cross-sectional area of the sample was 12.0mm 2 。
Tensile Strength after 10 ten thousand cycles (mN/mm) 2 ) =tensile strength (10 ten thousand times) (mN)/cross-sectional area (mm) of sample 2 )
The tensile strength after 10 ten thousand cycles is the ratio of the tensile strength under 10 ten thousand repeated loads to the cross-sectional area of the sample. The sheet having high tensile strength after 10 ten thousand cycles maintains high tensile strength even after 10 ten thousand loads, and is excellent in durability against repeated loads.
(mold Corrosion test)
20g of pellets were placed in a glass vessel (50 ml screw tube), and a metal column (5 mm square, 30mm in length) formed of HPM38 (Cr-plated) or HPM38 (Ni-plated) was suspended in the glass vessel so as not to contact the pellets. The glass container was then covered with aluminum foil. The glass container was put in an oven in this state and heated at 380℃for 3 hours. Then, the heated glass vessel was taken out of the oven, cooled to room temperature, and the degree of corrosion of the metal column surface was visually observed. The degree of corrosion was determined according to the following criteria.
O: no corrosion was observed
Delta: corrosion was slightly observed
X: corrosion was observed
(wire coating test)
By means ofA wire coating molding machine (manufactured by Takara Shuzo Co., ltd.) extruded a coating copolymer onto a copper conductor having a conductor diameter of 1.00mm at the following coating thickness to obtain a coated wire. The wire coating extrusion molding conditions were as follows.
a) Core conductor: conductor diameter 1.00mm
b) Coating thickness: 0.50mm
c) Coated wire diameter: 2.00mm
d) Wire drawing speed: 7 m/min
e) Extrusion conditions:
single screw extrusion moulding machine with barrel shaft diameter=20mm, l/d=22
Die (inner diameter)/sheet (outer diameter) =30.0 mm/10.0mm
Set temperature of extruder: barrel section C-1 (330 ℃), barrel section C-2 (360 ℃), barrel section C-3 (375 ℃), head section H (390 ℃), die section D-1 (405 ℃) and die section D-2 (395 ℃). The core wire preheating was set at 80 ℃.
(variation of outer diameter)
The outer diameter of the obtained coated wire was measured continuously for 1 hour using an outer diameter measuring instrument (ODAC 18XY manufactured by Zumbach Co.). The measured outer diameter value was rounded off from the predetermined outer diameter value (2.00 mm) by the third decimal point of the maximum outer diameter value, and the fluctuation value of the outer diameter was obtained. The ratio (change rate of the outer diameter) of the absolute value of the difference between the predetermined outer diameter and the change value of the outer diameter to the predetermined outer diameter (2.00 mm) was calculated, and the evaluation was performed according to the following criteria.
(change rate of outer diameter (%)) = | (change value of outer diameter) - (prescribed outer diameter) |/(prescribed outer diameter) ×100
1 percent: the change rate of the outer diameter is less than 1%
2% ± 2%: the change rate of the outer diameter exceeds 1% and is less than 2%
X: the change rate of the outer diameter exceeds 2 percent
(core wire Corrosion test)
The obtained coated wire was cut into a length of 20cm, left to stand in a constant temperature and humidity tank (fauc corporation, junior SD-01) at 60 ℃ and a humidity of 95% for 2 weeks, and then the coating layer was peeled off to expose the conductor, and the surface of the conductor was visually observed and evaluated according to the following criteria.
O: no corrosion was observed
X: corrosion was observed
(toner Release test)
UsingAn extruder (manufactured by hoku corporation) and a T-die, and a film was produced. Extrusion molding conditions were as follows.
a) Coiling speed: 1 m/min
b) Roller temperature: 120 DEG C
c) Film width: 70mm of
d) Thickness: 0.10mm
e) Extrusion conditions:
single screw extrusion moulding machine with cylinder axis diameter=14 mm and L/d=20
Set temperature of extruder: barrel section C-1 (330 ℃ C.), barrel section C-2 (350 ℃ C.), barrel section C-3 (370 ℃ C.), T die section (380 ℃ C.)
A50 mm by 50mm test piece was cut out from the obtained 0.10mm thick film, the obtained test piece was laid on a SUS bath, 3g of black toner powder was rolled up thereon into a round shape having a diameter of about 30mm, a lid of the bath was covered, and the bath was placed in a constant temperature bath heated to 160℃with the inside being a closed space. After 10 minutes, the cell was taken out, cooled to room temperature, and the test piece was taken out of the cell. The melt-cured product of the black toner was peeled from the test piece, and the peeled surface of the test piece was visually observed, and evaluated according to the following criteria.
O: no black deposit was observed on the peeled surface of the test piece
X: black deposit was observed on the peeled surface of the test piece
(abrasion test)
Using the pellets and a hot press molding machine, a sheet-like test piece having a thickness of about 0.2mm was produced, from which a 10 cm. Times.10 cm test piece was cut. The test piece thus prepared was fixed to a test stand of a taber abrasion tester (taber abrasion tester, model No.101, manufactured by An Tian refiner manufacturing company), and abrasion test was performed using the taber abrasion tester under conditions of a load of 500g, abrasion wheel CS-10 (20 revolutions ground with grinding paper # 240), and a rotation speed of 60 rpm. The weight of the test piece after 1000 revolutions was measured, and the test piece weight was further measured after 10000 revolutions with the same test piece. The abrasion loss was determined by the following formula.
Abrasion loss (mg) =m1-M2
M1: test piece weight after 1000 revolutions (mg)
M2: test piece weight after 10000 revolutions (mg)
(carbon dioxide permeability coefficient)
A sheet-like test piece having a thickness of about 0.1mm was produced using the pellets and a hot press molding machine. Using the obtained test piece, the test piece was prepared according to JIS K7126-1:2006, carbon dioxide permeation was measured using a differential pressure type gas permeation rate meter (L100-5000 type gas permeation rate meter, manufactured by Systemech ilinois Co.). Obtaining a permeation area of 50.24cm 2 The carbon dioxide permeability at a test temperature of 70℃and a test humidity of 0% RH. Using the obtained carbon dioxide permeation rate and the thickness of the test piece, the carbon dioxide permeation coefficient was calculated by the following formula.
Carbon dioxide permeability coefficient (cm) 3 ·mm/(m 2 ·24h·atm))＝GTR×d
GTR: carbon dioxide permeability (cm) 3 /(m 2 ·24h·atm))
d: test piece thickness (mm)
(electrolyte permeability)
A sheet-like test piece having a thickness of about 0.2mm was produced using the pellets and a hot press molding machine. In a test cup (permeation area 12.56 cm) 2 ) 10g of dimethyl carbonate (DMC) was placed therein, covered with a sheet-like test piece, and fastened and sealed with a PTFE gasket interposed therebetween. The pellet was allowed to contact DMC, kept at 60℃for 30 days, and then taken out, and left at room temperature for 1 hour to measure the mass reduction. The DMC permeability (g.cm/m) was determined by 2 )。
Electrolyte permeability (g.cm/m) 2 ) =mass reduction amount (g) ×thickness (cm)/transmission area (m) of sheet-like test piece 2 )
(tube formability)
Using the pellets obtained in the examplesAn extrusion molding machine (field plastic machine manufacturing) extrusion-molded a tube having an outer diameter of 10.0mm and a wall thickness of 1.0 mm.
Extrusion molding conditions were as follows.
a) Die inside diameter: 20mm of
b) Mandrel outside diameter: 13mm of
c) Sizing die inner diameter: 10.5mm
d) Traction speed: 0.4 m/min
e) Outer diameter: 10.0mm
f) Wall thickness: 1.0mm
g) Extrusion conditions:
single screw extrusion moulding machine with cylinder shaft diameter=30 mm, L/d=22
Set temperature of extruder: barrel part C-1 (330 ℃ C.), barrel part C-2 (365 ℃ C.), barrel part C-3 (380 ℃ C.), head part H-1 (380 ℃ C.), die part D-1 (390 ℃ C.), die part D-2 (390 ℃ C.)
The obtained tube was observed and evaluated according to the following criteria. The appearance of the tube was visually confirmed.
O: good appearance
X: the cross section was not circular, and the appearance was poor due to flattening, uneven thickness, and the like.
(dielectric loss tangent)
The pellets were melt-molded to prepare a cylindrical test piece having a diameter of 2 mm. The test piece thus fabricated was set in a cavity resonator for 6GHz manufactured by kanto electronics application development company, and measured by a network analyzer manufactured by agilent technologies. The measurement result was analyzed by analysis software "CPMA" manufactured by Kanto electronic application development Co., ltd. On a personal computer connected to the network analyzer, to thereby determine the dielectric loss tangent (tan. Delta.) at 20℃and 6 GHz.
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Claims (5)

1. A copolymer comprising tetrafluoroethylene units and perfluoro (propyl vinyl ether) units,
the content of perfluoro (propyl vinyl ether) units is 2.26 to 2.75 mol% relative to the total monomer units,
The melt flow rate at 372 ℃ is 4.0g/10 min-11.0 g/10 min,
the number of functional groups per 10 6 The number of carbon atoms of the main chain is 50 or less.
2. The copolymer of claim 1, wherein the melt flow rate at 372 ℃ is from 5.0g/10 min to 10.0g/10 min.
3. An injection molded article comprising the copolymer according to claim 1 or 2.
4. A coated wire comprising a coating layer comprising the copolymer according to claim 1 or 2.
5. A molded body comprising the copolymer according to claim 1 or 2, wherein the molded body is a filter housing, a film, a bottle, a wire coating, or a tube.
CN202280016007.5A 2021-02-26 2022-01-31 Copolymer, molded body, injection molded body, and coated electric wire Pending CN116964113A (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP2021-031088 2021-02-26
JP2021-162115 2021-09-30
JP2021162115 2021-09-30
PCT/JP2022/003636 WO2022181222A1 (en) 2021-02-26 2022-01-31 Copolymer, molded body, injection molded body, and coated electrical wire

Publications (1)

Publication Number Publication Date
CN116964113A true CN116964113A (en) 2023-10-27

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN202280016007.5A Pending CN116964113A (en) 2021-02-26 2022-01-31 Copolymer, molded body, injection molded body, and coated electric wire

Country Status (1)

Country Link
CN (1) CN116964113A (en)

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