Patent Application
20230399439
The present disclosure relates to a fluorine-containing copolymer.
Patent Literature 1 describes a terpolymer containing (a) tetrafluoroethylene, (b) hexafluoropropylene in an amount of about 4 to about 12% by weight based on the weight of the terpolymer, and (c) perfluoro(ethyl vinyl ether) or perfluoro(n-propyl vinyl ether) in an amount of about 0.5 to about 3% by weight based on the weight of the terpolymer, in a copolymerized form.
According to the present disclosure, there is provided a fluorine-containing copolymer comprising tetrafluoroethylene unit, hexafluoropropylene unit and perfluoro(propyl vinyl ether) unit, wherein the copolymer has a content of hexafluoropropylene unit of 7.0 to 8.5% by mass with respect to the whole of the monomer units, a content of perfluoro(propyl vinyl ether) unit of 1.5 to 2.9% by mass with respect to the whole of the monomer units, and a melt flow rate at 372° C. of 9 to 15 g/10 min.
According to the present disclosure, there can be provided a fluorine-containing copolymer which can give a beautiful injection molded article by being molded at a high injection rate by an injection molding method, can form a thin coating layer on a core wire having a small diameter at a high rate by an extrusion forming method, can be formed into a film uniform in thickness at a high extrusion rate by an extrusion forming method, and can give a formed article excellent in the 50° C. abrasion resistance, the low hydrogen permeation, the 75° C. high-temperature rigidity, the 140° C. tensile creep resistance and the solvent crack resistance.
Hereinafter, specific embodiments of the present disclosure will be described in detail, but the present disclosure is not limited to the following embodiments.
A fluorine-containing copolymer of the present disclosure comprises tetrafluoroethylene (TFE) unit, hexafluoropropylene (HFP) unit and perfluoro(propyl vinyl ether) (PPVE) unit.
As fluororesins, non melt-processible fluororesins such as polytetrafluoroethylene (PTFE), and melt-fabricable fluororesins are known. PTFE, though having excellent properties, has such a drawback that the melt processing is remarkably difficult. Meanwhile, as the melt-fabricable fluororesins, TFE/HFP copolymers (FEP), TFE/PPVE copolymers (PFA) and the like are known; however, these have a drawback of being inferior in the heat resistance and the like to PTFE. Then, Patent Literature 1 proposes the above-mentioned terpolymer as a fluorocarbon polymer improved in these drawbacks.
However, a fluorine-containing copolymer is demanded that is better in the moldability and can a give formed article better in the 50° C. abrasion resistance, the low hydrogen permeation, the 75° C. high-temperature rigidity, the 140° C. tensile creep resistance and the solvent crack resistance, than the conventional copolymer. For example, for valves to control the pressure and the flow amount of fluids such as chemical solutions, high-temperature abrasion resistance, high-temperature rigidity and the tensile creep resistance are demanded so that damage is not produced by the friction, the tensile stress, the load and the like generated in opening and closing of the valves. Further, since some of those valves have a complex structure having thin-wall portions, good moldability is demanded for the copolymer.
It has been found that by regulating, in very limited ranges, the contents of HFP unit and PPVE unit and the melt flow rate of the fluorine-containing copolymer containing TFE unit, HFP unit and PPVE unit, the moldability of the fluorine-containing copolymer is remarkably improved and there can be obtained a formed article excellent in the 50° C. abrasion resistance, the low hydrogen permeation, the 75° C. high-temperature rigidity, the 140° C. tensile creep resistance and the solvent crack resistance.
Moreover, by forming the fluorine-containing copolymer of the present disclosure by an extrusion forming method, a thin coating layer can be formed at a high rate on a core wire having a small diameter, or the fluorine-containing copolymer can be formed at a high forming rate into a thin film uniform in thickness. Thus, the fluorine-containing copolymer of the present disclosure can be utilized not only as a material for valves, but also can be utilized in the broad fields such as electric wire coatings and films.
The fluorine-containing copolymer of the present disclosure is a melt-fabricable fluororesin. Being melt-fabricable means that a polymer can be melted and processed by using a conventional processing device such as an extruder or an injection molding machine.
The content of the HFP unit of the fluorine-containing copolymer is, with respect to the whole of the monomer units, 7.0 to 8.5% by mass, and preferably 7.1% by mass or higher, more preferably 7.2% by mass or higher and still more preferably 7.4% by mass or higher, and preferably 8.4% by mass or lower, more preferably 8.3% by mass or lower, still more preferably 8.2% by mass or lower, further still more preferably 8.1% by mass or lower, especially preferably 7.9% by mass or lower and most preferably 7.7% by mass. When the content of the HFP unit is too high, formed articles excellent in the 75° C. high-temperature rigidity and the 140° C. tensile creep resistance cannot be obtained; and when the content of the HFP unit is too low, formed articles excellent in the 50° C. abrasion resistance and the solvent crack resistance cannot be obtained.
The content of the PPVE unit of the fluorine-containing copolymer is, with respect to the whole of the monomer units, 1.5 to 2.9% by mass, and preferably 1.6% by mass or higher, more preferably 1.7% by mass or higher, still more preferably 1.8% by mass or higher, especially preferably 1.9% by mass or higher and most preferably 2.0% by mass or higher, and preferably 2.8% by mass or lower, more preferably 2.7% by mass or lower, still more preferably 2.6% by mass or lower, further still more preferably 2.5% by mass or lower, further still more preferably 2.4% by mass or lower, especially preferably 2.3% by mass or lower and most preferably 2.2% by mass or lower. Due to that the content of the PPVE unit of the fluorine-containing copolymer is in the above range, there can be obtained formed articles excellent in the 50° C. abrasion resistance, the low hydrogen permeation, the 75° C. high-temperature rigidity, the 140° C. tensile creep resistance and the solvent crack resistance. When the content of the PPVE unit is too low, formed articles excellent in the 50° C. abrasion resistance and the solvent crack resistance cannot be obtained.
The content of the TFE unit of the fluorine-containing copolymer is, with respect to the whole of the monomer units, preferably 88.6 to 91.5% by mass, and more preferably 88.8% by mass or higher, still more preferably 88.9% by mass or higher, further still more preferably 89.0% by mass or higher, especially preferably 89.3% by mass or higher and most preferably 89.7% by mass or higher, and more preferably 91.7% by mass or lower, still more preferably 91.4% by mass or lower, further still more preferably 91.3% by mass or lower, especially preferably 91.1% by mass or lower and most preferably 90.8% by mass or lower. Then, the content of the TFE unit may be selected so that the total of contents of the HFP unit, the PPVE unit, the TFE unit and other monomer units becomes 100% by mass.
The fluorine-containing copolymer of the present disclosure is not limited as long as the copolymer contains the above three monomer units, and may be a copolymer containing only the above three monomer units, or may be a copolymer containing the above three monomer units and other monomer units.
The other monomers are not limited as long as being copolymerizable with TFE, HFP and PPVE, and may be fluoromonomers or fluorine-non-containing monomers.
It is preferable that the fluoromonomer is at least one selected from the group consisting of chlorotrifluoroethylene, vinyl fluoride, vinylidene fluoride, trifluoroethylene, hexafluoroisobutylene, monomers represented by CH2═CZ1(CF2)nZ2 (wherein Z1 is H or F, Z2 is H, F or Cl, and n is an integer of 1 to 10), perfluoro(alkyl vinyl ether)s [PAVE] represented by CF2═CF—ORf1 (wherein Rf1 is a perfluoroalkyl group having 1 to 8 carbon atoms) (here, excluding PPVE), alkyl perfluorovinyl ether derivatives represented by CF2═CFO—CH2—Rf2 (wherein Rf2 is a perfluoroalkyl group having 1 to 5 carbon atoms), perfluoro-2,2-dimethyl-1,3-dioxol [PDD], and perfluoro-2-methylene-4-methyl-1,3-dioxolane [PMD].
The monomers represented by CH2═CZ1(CF2)nZ2 include CH2═CFCF3, CH2═CH—C4F9, CH2═CH—C6F13, and CH2═CF—C3F6H.
The perfluoro(alkyl vinyl ether)s represented by CF2═CF—ORf1 include CF2═CF—OCF3 and CF2═CF—OCF2CF3.
The fluorine-non-containing monomers include hydrocarbon-based monomers copolymerizable with TFE, HFP and PPVE. Examples of the hydrocarbon-based monomers include alkenes such as ethylene, propylene, butylene, and isobutylene; alkyl vinyl ethers such as ethyl vinyl ether, propyl vinyl ether, butyl vinyl ether, isobutyl vinyl ether, and cyclohexyl vinyl ether; vinyl esters such as vinyl acetate, vinyl propionate, n-vinyl butyrate, vinyl isobutyrate, vinyl valerate, vinyl pivalate, vinyl caproate, vinyl caprylate, vinyl caprate, vinyl versatate, vinyl laurate, vinyl myristate, vinyl palmitate, vinyl stearate, vinyl benzoate, vinyl para-t-butylbenzoate, vinyl cyclohexanecarboxylate, vinyl monochloroacetate, vinyl adipate, vinyl acrylate, vinyl methacrylate, vinyl crotonate, vinyl sorbate, vinyl cinnamate, vinyl undecylenate, vinyl hydroxyacetate, vinyl hydroxypropionate, vinyl hydroxybutyrate, vinyl hydroxyvalerate, vinyl hydroxyisobutyrate, and vinyl hydroxycyclohexanecarboxylate; alkyl allyl ethers such as ethyl allyl ether, propyl allyl ether, butyl allyl ether, isobutyl allyl ether, and cyclohexyl allyl ether; and alkyl allyl esters such as ethyl allyl ester, propyl allyl ester, butyl allyl ester, isobutyl allyl ester, and cyclohexyl allyl ester.
The fluorine-non-containing monomers may also be functional group-containing hydrocarbon-based monomers copolymerizable with TFE, HFP and PPVE. Examples of the functional group-containing hydrocarbon-based monomers include hydroxyalkyl vinyl ethers such as hydroxyethyl vinyl ether, hydroxypropyl vinyl ether, hydroxybutyl vinyl ether, hydroxyisobutyl vinyl ether, and hydroxycyclohexyl vinyl ether; fluorine-non-containing monomers having a glycidyl group, such as glycidyl vinyl ether and glycidyl allyl ether; fluorine-non-containing monomers having an amino group, such as aminoalkyl vinyl ethers and aminoalkyl allyl ethers; fluorine-non-containing monomers having an amido group, such as (meth)acrylamide and methylolacrylamide; bromine-containing olefins, iodine-containing olefins, bromine-containing vinyl ethers, and iodine-containing vinyl ethers; and fluorine-non-containing monomers having a nitrile group.
The content of the other monomer units in the fluorine-containing copolymer of the present disclosure is, with respect to the whole of the monomer units, preferably 0 to 2.9% by mass, and more preferably 1.4% by mass or lower, still more preferably 1.0% by mass or lower, further still more preferably 0.5% by mass or lower and especially preferably 0.1% by mass or lower.
The melt flow rate (MFR) of the fluorine-containing copolymer is 9 to 15 g/10 min, and preferably 9.1 g/10 min or higher, more preferably 9.6 g/10 min or higher, still more preferably 10 g/10 min or higher and especially preferably 10.8 g/10 min or higher, and preferably 14 g/10 min or lower, more preferably 13 g/10 min or lower and still more preferably 12 g/10 min or lower. Due to that the MFR of the fluorine-containing copolymer is in the above range, the moldability of the copolymer is improved and there can be obtained formed articles excellent in the 50° C. abrasion resistance, the low hydrogen permeation, the 75° C. high-temperature rigidity, the 140° C. tensile creep resistance and the solvent crack resistance. When the MFR is too low, formed articles excellent in the low hydrogen permeation and the 75° C. high-temperature rigidity cannot be obtained; and when the MFR is too high, formed articles excellent in the 50° C. abrasion resistance, the 140° C. tensile creep resistance and the solvent crack resistance cannot be obtained.
In the present disclosure, the MFR is a value obtained as a mass (g/10 min) of a polymer flowing out from a die of 2 mm in inner diameter and 8 mm in length per 10 min at 372° C. under a load of 5 kg using a melt indexer G-01 (manufactured by Toyo Seiki Seisaku-sho Ltd.), according to ASTM D1238.
The MFR can be regulated by regulating the kind and amount of a polymerization initiator to be used in polymerization of monomers, the kind and amount of a chain transfer agent, and the like.
The fluorine-containing copolymer of the present disclosure may or may not have functional groups. The functional groups are functional groups present on the main chain terminals or side chain terminals of the fluorine-containing copolymer, and functional groups present on the main chain or side chains thereof. Typical functional groups are —CF═CF2, —CF2H, —COF, —COOH, —COOCH3, —CONH2 and —CH2OH.
The number of functional groups per 106 main-chain carbon atoms of the fluorine-containing copolymer is preferably 90 or less, more preferably 70 or less, still more preferably 50 or less, further still more preferably 40 or less, further still more preferably 30 or less, especially preferably 20 or less and most preferably less than 15. Due to that the number of functional groups of the fluorine-containing copolymer is in the above range, there can be obtained formed articles hardly making fluorine ions to dissolve out in chemical solutions such as a hydrogen peroxide aqueous solution.
The number of functional groups of the fluorine-containing copolymer is the total number of —CF═CF2, —CF2H, —COF, —COOH, —COOCH3, —CONH2 and —CH2OH.
The number of —CF2H per 106 main-chain carbon atoms of the fluorine-containing copolymer is preferably 50 or less, more preferably 40 or less, still more preferably 30 or less, further still more preferably 20 or less, especially preferably less than 15 and most preferably 10 or less.
The total number of —COOH, —COOCH3, —CH2OH, —COF, —CF═CF2 and —CONH2 per 106 main-chain carbon atoms of the fluorine-containing copolymer is preferably 80 or less, more preferably 70 or less, still more preferably 50 or less, further still more preferably 40 or less, further still more preferably 30 or less, especially preferably 20 or less and most preferably less than 15.
For identification of the kind of the functional groups and measurement of the number of the functional groups, infrared spectroscopy can be used.
The number of the functional groups is measured, specifically, by the following method. First, the fluorine-containing copolymer is molded by cold press to prepare a film of 0.25 to 0.30 mm in thickness. The film is analyzed by Fourier transform infrared spectroscopy to obtain an infrared absorption spectrum, and a difference spectrum against a base spectrum that is completely fluorinated and has no functional groups is obtained. From an absorption peak of a specific functional group observed on this difference spectrum, the number N of the functional group per 1×106 carbon atoms in the fluorine-containing copolymer is calculated according to the following formula (A).
N=I×K/t (A)
For reference, for some functional groups, the absorption frequency, the molar absorption coefficient and the correction factor are shown in Table 1. Then, the molar absorption coefficients are those determined from FT-IR measurement data of low molecular model compounds.
Absorption frequencies of —CH2CF2H, —CH2COF, —CH2COOH, —CH2COOCH3 and —CH2CONH2 are lower by a few tens of kaysers (cm−1) than those of —CF2H, —COF, —COOH free and —COOH bonded, —COOCH3 and —CONH2 shown in the Table, respectively.
For example, the number of the functional group —COF is the total of the number of a functional group determined from an absorption peak having an absorption frequency of 1,883 cm−1 derived from —CF2COF and the number of a functional group determined from an absorption peak having an absorption frequency of 1,840 cm−1 derived from —CH2COF.
The number of —CF2H groups can also be determined from a peak integrated value of the —CF2H group acquired in a 19F-NMR measurement using a nuclear magnetic resonance spectrometer and set at a measurement temperature of (the melting point of a polymer+20)° C.
The functional groups are functional groups present on the main chain terminals or side chain terminals of the fluorine-containing copolymer, and functional groups present on the main chain or side chains thereof. The number of functional groups may be the total number of —CF═CF2, —CF2H, —COF, —COOH, —COOCH3, —CONH2 and —CH2OH.
The functional groups are introduced to the fluorine-containing copolymer, for example, by a chain transfer agent or a polymerization initiator used in production of the fluorine-containing copolymer. For example, in the case of using an alcohol as the chain transfer agent, or a peroxide having a structure of —CH2OH as the polymerization initiator, —CH2OH is introduced on the main chain terminals of the fluorine-containing copolymer. Alternatively, the functional group is introduced on the side chain terminal of the fluorine-containing copolymer by polymerizing a monomer having the functional group.
By subjecting the fluorine-containing copolymer having such functional groups to a treatment such as a wet heat treatment, a fluorination treatment or the like, there can be obtained the fluorine-containing copolymer having the number of functional groups in the above range. The fluorine-containing copolymer is preferably one having been subjected to a wet heat treatment or a fluorination treatment, and more preferably one having been subjected to a fluorination treatment. It is also preferable that the fluorine-containing copolymer of the present disclosure has a —CF3 terminal group.
The melting point of the fluorine-containing copolymer is preferably 250 to 285° C. and more preferably 260 to 272° C. Due to that the melting point is in the above range, the moldability of the copolymer is more improved, and there can be obtained formed articles better in the 50° C. abrasion resistance, the low hydrogen permeation, the 75° C. high-temperature rigidity, the 140° C. tensile creep resistance and the solvent crack resistance.
In the present disclosure, the melting point can be measured by using a differential scanning calorimeter [DSC].
The hydrogen permeation coefficient of the fluorine-containing copolymer is preferably 1,790 cm3·mm//(m2·24 h·atm) or lower. The fluorine-containing copolymer of the present disclosure has an excellent low hydrogen permeation, due to suitably regulated contents of the HFP unit and the PPVE unit, and melt flow rate. Hence, tanks obtained by using the fluorine-containing copolymer of the present disclosure can suitably be used for storage of chemical solutions disliking contamination with hydrogen in the outside air.
In the present disclosure, the hydrogen permeation coefficient can be measured under the condition of a test temperature of 60° C. and a test humidity of 0% RH. The specific measurement of the hydrogen permeation coefficient can be carried out by a method described in Examples.
In the fluorine-containing copolymer of the present disclosure, the amount of fluorine ions dissolving out therefrom detected by an immersion test in a hydrogen peroxide aqueous solution is, in terms of mass, preferably 4.0 ppm or lower, more preferably 3.0 ppm or lower and still more preferably 2.8 ppm or lower.
In the present disclosure, the immersion test in a hydrogen peroxide aqueous solution can be carried out by using the fluorine-containing copolymer and preparing a test piece having a weight corresponding to that of 10 sheets of a formed article (15 mm×15 mm×0.2 mm), and putting, in a thermostatic chamber of 95° C., a polypropylene-made bottle in which the test piece and 15 g of a 3-mass % hydrogen peroxide aqueous solution are put and allowing the resultant to stand for 20 hours.
The fluorine-containing copolymer of the present disclosure can be produced by any polymerization method of bulk polymerization, suspension polymerization, solution polymerization, emulsion polymerization and the like. In these polymerization methods, conditions such as temperature and pressure, a polymerization initiator, a chain transfer agent, a solvent and other additives can suitably be set depending on the composition and the amount of a desired fluorine-containing copolymer.
The polymerization initiator may be an oil-soluble radical polymerization initiator or a water-soluble radical initiator.
An oil-soluble radical polymerization initiator may be a known oil-soluble peroxide, and examples thereof typically include:
The di[fluoro(or fluorochloro)acyl] peroxides include diacyl peroxides represented by [(RfCOO)—]2 wherein Rf is a perfluoroalkyl group, an ω-hydroperfluoroalkyl group or a fluorochloroalkyl group.
Examples of the di[fluoro(or fluorochloro)acyl]peroxides include di(ω)-hydro-dodecafluorohexanoyl) peroxide, di(ω)-hydro-tetradecafluoroheptanoyl) peroxide, di(ω)-hydro-hexadecafluorononanoyl) peroxide, di(perfluorobutyryl) peroxide, di(perfluorovaleryl) peroxide, di(perfluorohexanoyl) peroxide, di(perfluoroheptanoyl) peroxide, di(perfluorooctanoyl) peroxide, di(perfluorononanoyl) peroxide, di(ω)-chloro-hexafluorobutyryl) peroxide, di(ω)-chloro-decafluorohexanoyl) peroxide, di(ω)-chloro-tetradecafluorooctanoyl) peroxide, ω-hydrodo-decafluoroheptanoyl-ω-hydrohexadecafluorononanoyl peroxide, ω-chloro-hexafluorobutyryl-ω-chloro-decafluorohexanoyl peroxide, ω-hydrododecafluoroheptanoyl-perfluorobutyryl peroxide, di(dichloropentafluorobutanoyl) peroxide, di(trichlorooctafluorohexanoyl) peroxide, di(tetrachloroundecafluorooctanoyl) peroxide, di(pentachlorotetradecafluorodecanoyl) peroxide and di(undecachlorotriacontafluorodocosanoyl) peroxide.
The water-soluble radical polymerization initiator may be a well known water-soluble peroxide, and examples thereof include ammonium salts, potassium salts and sodium salts of persulfuric acid, perboric acid, perchloric acid, perphosphoric acid, percarbonic acid and the like, and t-butyl permaleate and t-butyl hydroperoxide. A reductant such as a sulfite salt may be combined with a peroxide and used, and the amount thereof to be used may be 0.1 to 20 times with respect to the peroxide.
Examples of the chain transfer agent include hydrocarbons such as ethane, isopentane, n-hexane and cyclohexane; aromatics such as toluene and xylene; ketones such as acetone; acetates such as ethyl acetate and butyl acetate; alcohols such as methanol, ethanol and 2,2,2-trifluoroethanol; mercaptans such as methyl mercaptan; halogenated hydrocarbons such as carbon tetrachloride, chloroform, methylene chloride and methyl chloride; and 3-fluorobenzotrifluoride. The amount thereof to be added can vary depending on the magnitude of the chain transfer constant of a compound to be used, but the chain transfer agent is used usually in the range of 0.01 to 20 parts by mass with respect to 100 parts by mass of a solvent.
For example, in the cases of using a dialkyl peroxycarbonate, a di[fluoro(or fluorochloro)acyl] peroxide or the like as a polymerization initiator, although there are some cases where the molecular weight of an obtained fluorine-containing copolymer becomes too high and the regulation of the melt flow rate to a desired one is not easy, the molecular weight can be regulated by using the chain transfer agent. It is especially suitable that the fluorine-containing copolymer is produced by suspension polymerization using the chain transfer agent such as an alcohol and the oil-soluble radical polymerization initiator.
The solvent includes water and mixed solvents of water and an alcohol. A monomer to be used for the polymerization of the fluorine-containing copolymer of the present disclosure can also be used as the solvent.
In the suspension polymerization, in addition to water, a fluorosolvent may be used. The fluorosolvent may include hydrochlorofluoroalkanes such as CH3CClF2, CH3CCl2F, CF3CF2CCl2H and CF2ClCF2CFHCl; chlorofluoroalaknes such as CF2ClCFClCF2CF3 and CF3CFClCFClCF3; and perfluoroalkanes such as perfluorocyclobutane, CF3CF2CF2CF3, CF3CF2CF2CF2CF3 and CF3CF2CF2CF2CF2CF3, and among these, perfluoroalkanes are preferred. The amount of the fluorosolvent to be used is, from the viewpoint of the suspensibility and the economic efficiency, preferably 10 to 100 parts by mass with respect to 100 parts by mass of the solvent.
The polymerization temperature is not limited, and may be 0 to 100° C. In the case where the decomposition rate of the polymerization initiator is too high, including cases of using a dialkyl peroxycarbonate, a di[fluoro(or fluorochloro)acyl]peroxide or the like as the polymerization initiator, it is preferable to adopt a relatively low polymerization temperature such as in the temperature range of 0 to 35° C.
The polymerization pressure can suitably be determined according to other polymerization conditions such as the kind of the solvent to be used, the amount of the solvent, the vapor pressure and the polymerization temperature, but usually may be 0 to 9.8 MPaG. The polymerization pressure is preferably 0.1 to 5 MPaG, more preferably 0.5 to 2 MPaG and still more preferably 0.5 to 1.5 MPaG. When the polymerization pressure is 1.5 MPaG or higher, the production efficiency can be improved.
Examples of the additives in the polymerization include suspension stabilizers. The suspension stabilizers are not limited as long as being conventionally well-known ones, and methylcellulose, polyvinyl alcohols and the like can be used. With the use of a suspension stabilizer, suspended particles produced by the polymerization reaction are dispersed stably in an aqueous medium, and therefore the suspended particles hardly adhere on the reaction vessel even when a SUS-made reaction vessel not having been subjected to adhesion preventing treatment such as glass lining is used. Accordingly, a reaction vessel withstanding a high pressure can be used, and therefore the polymerization under a high pressure becomes possible and the production efficiency can be improved. By contrast, in the case of carrying out the polymerization without using the suspension stabilizer, the suspended particles may adhere and the production efficiency may be lowered with the use of a SUS-made reaction vessel not having been subjected to adhesion preventing treatment is used. The concentration of the suspension stabilizer in the aqueous medium can suitably be regulated depending on conditions.
In the case of obtaining an aqueous dispersion containing a fluoropolymer by a polymerization reaction, a dried fluoropolymer may be recovered by coagulating, cleaning and drying the fluorine-containing copolymer contained in the aqueous dispersion. Alternatively, in the case of obtaining the fluorine-containing copolymer as a slurry by a polymerization reaction, a dried fluoropolymer may be recovered by taking out the slurry from a reaction vessel, and cleaning and drying the slurry. The fluorine-containing copolymer can be recovered in a powder form by the drying.
The fluorine-containing copolymer obtained by the polymerization may be formed into pellets. A method of forming into pellets is not limited, and a conventionally known method can be used. Examples thereof include methods of melt extruding the fluorine-containing copolymer by using a single-screw extruder, a twin-screw extruder or a tandem extruder and cutting the resultant into a predetermined length to form the fluorine-containing copolymer into pellets. The extrusion temperature in the melt extrusion needs to be varied depending on the melt viscosity and the production method of the fluorine-containing copolymer, and is preferably the melting point of the fluorine-containing copolymer+20° C. to the melting point of the fluorine-containing copolymer+140° C. A method of cutting the fluorine-containing copolymer is not limited, and there can be adopted a conventionally known method such as a strand cut method, a hot cut method, an underwater cut method, or a sheet cut method. Volatile components in the obtained pellets may be removed by heating the pellets (degassing treatment). Alternatively, the obtained pellets may be treated by bringing the pellets into contact with hot water of 30 to 200° C., steam of 100 to 200° C. or hot air of 40 to 200° C.
The fluorine-containing copolymer obtained by the polymerization may be heated in the presence of air and water at a temperature of 100° C. or higher (wet heat treatment). Examples of the wet heat treatment include a method in which by using an extruder, the fluorine-containing copolymer obtained by the polymerization is melted and extruded while air and water are fed. The wet heat treatment can convert thermally unstable functional groups of the fluorine-containing copolymer, such as —COF and —COOH, to thermally relatively stable —CF2H, whereby the total number of —COF and —COOH and the total number of —COOH, —COOCH3, —CH2OH, —COF, —CF═CF2, and —CONH2 of the fluorine-containing copolymer can easily be regulated in the above-mentioned ranges. By heating the fluorine-containing copolymer, in addition to air and water, in the presence of an alkali metal salt, the conversion reaction to —CF2H can be promoted. Depending on applications of the fluorine-containing copolymer, however, it should be paid regard to that contamination by the alkali metal salt must be avoided.
The fluorine-containing copolymer obtained by polymerization may be subjected to a fluorination treatment. The fluorination treatment can be carried out by bringing the fluorine-containing copolymer subjected to no fluorination treatment into contact with a fluorine-containing compound. The fluorination treatment can convert thermally unstable functional groups of the fluorine-containing copolymer, such as —COOH, —COOCH3, —CH2OH, —COF, —CF═CF2 and —CONH2, and thermally relatively stable functional groups thereof, such as —CF2H, to thermally very stable —CF3. Resultantly, the total number of —COOH, —COOCH3, —CH2OH, —COF, —CF═CF2, —CONH2 and —CF2H can easily be regulated in the above-mentioned ranges.
The fluorine-containing compound is not limited, but includes fluorine radical sources generating fluorine radicals under the fluorination treatment condition. The fluorine radical sources include F2 gas, CoF3, AgF2, UF6, OF2, N2F2, CF3OF, halogen fluorides (for example, IF5 and ClF3).
The fluorine radical source such as F2 gas may be, for example, one having a concentration of 100%, but from the viewpoint of safety, the fluorine radical source is preferably mixed with an inert gas and diluted therewith to 5 to 50% by mass, and then used; and it is more preferably to be diluted to 15 to 30% by mass. The inert gas includes nitrogen gas, helium gas and argon gas, but from the viewpoint of the economic efficiency, nitrogen gas is preferred.
The condition of the fluorination treatment is not limited, and the fluorine-containing copolymer in a melted state may be brought into contact with the fluorine-containing compound, but the fluorination treatment can be carried out usually at a temperature of not higher than the melting point of the fluorine-containing copolymer, preferably at 20 to 220° C. and more preferably at 100 to 200° C. The fluorination treatment is carried out usually for 1 to 30 hours and preferably 5 to 25 hours. The fluorination treatment is preferred which brings the fluorine-containing copolymer having been subjected to no fluorination treatment into contact with fluorine gas (F2 gas).
A composition may be obtained by mixing the fluorine-containing copolymer of the present disclosure and as required, other components. The other components include fillers, plasticizers, processing aids, mold release agents, pigments, flame retarders, lubricants, light stabilizers, weathering stabilizers, electrically conductive agents, antistatic agents, ultraviolet absorbents, antioxidants, foaming agents, perfumes, oils, softening agents and dehydrofluorination agents.
Examples of the fillers include silica, kaolin, clay, organo clay, talc, mica, alumina, calcium carbonate, calcium terephthalate, titanium oxide, calcium phosphate, calcium fluoride, lithium fluoride, crosslinked polystyrene, potassium titanate, carbon, boron nitride, carbon nanotube and glass fiber. The electrically conductive agents include carbon black. The plasticizers include dioctyl phthalate and pentaerythritol. The processing aids include carnauba wax, sulfone compounds, low molecular weight polyethylene and fluorine-based auxiliary agents. The dehydrofluorination agents include organic oniums and amidines.
Then, the other components may be other polymers other than the above-mentioned fluorine-containing copolymer. The other polymers include fluororesins other than the above fluorine-containing copolymer, fluoroelastomers and non-fluorinated polymers.
A method of producing the above composition includes a method in which the fluorine-containing copolymer and other components are dry mixed, and a method in which the fluorine-containing copolymer and other components are previously mixed by a mixer, and then, melt kneaded by a kneader, a melt extruder or the like.
The fluorine-containing copolymer of the present disclosure or the above-mentioned composition can be used as a processing aid, a forming material or the like, but it is suitable to use that as a forming material. Then, aqueous dispersions, solutions and suspensions of the fluorine-containing copolymer of the present disclosure, and the copolymer/solvent-based materials can also be utilized; and these can be used for application of coating materials, encapsulation, impregnation, and casting of films. However, since the fluorine-containing copolymer of the present disclosure has the above-mentioned properties, it is preferable to use the copolymer as the forming material.
Formed articles may be obtained by forming the fluorine-containing copolymer of the present disclosure or the above-mentioned composition.
A method of forming the fluorine-containing copolymer or the composition is not limited, and includes injection molding, extrusion forming, compression molding, blow molding, transfer molding, rotomolding and rotolining molding. As the forming method, among these, preferable are extrusion forming, compression molding, injection molding and transfer molding; from the viewpoint of being able to produce forming articles in a high productivity, more preferable are injection molding, extrusion forming and transfer molding, and still more preferable is injection molding. That is, it is preferable that formed articles are extrusion formed articles, compression molded articles, injection molded articles or transfer molded articles; and from the viewpoint of being able to produce molded articles in a high productivity, being injection molded articles, extrusion formed articles or transfer molded articles is more preferable, and being injection molded articles is still more preferable. By forming the fluorine-containing copolymer of the present disclosure by an injection molding method, beautiful formed articles can be obtained even in the case of molding at a high injection rate.
Formed articles containing the fluorine-containing copolymer of the present disclosure may be, for example, nuts, bolts, joints, films, bottles, gaskets, electric wire coatings, tubes, hoses, pipes, valves, sheets, seals, packings, tanks, rollers, containers, cocks, connectors, filter housings, filter cages, flowmeters, pumps, wafer carriers, and wafer boxes.
The fluorine-containing copolymer of the present disclosure, the above composition and the above formed articles can be used, for example, in the following applications.
Food packaging films, and members for liquid transfer for food production apparatuses, such as lining materials of fluid transfer lines, packings, sealing materials and sheets, used in food production processes;
The fuel transfer members used in fuel systems of automobiles further include fuel hoses, filler hoses and evap hoses. The above fuel transfer members can also be used as fuel transfer members for gasoline additive-containing fuels, resultant to sour gasoline, resultant to alcohols, and resultant to methyl tertiary butyl ether and amines and the like.
The above chemical stoppers and packaging films for chemicals have excellent chemical resistance to acids and the like. The above chemical solution transfer members also include corrosion proof tapes wound on chemical plant pipes.
The above formed articles also include vehicular radiator tanks, chemical solution tanks, bellows, spacers, rollers and gasoline tanks, waste solution transport containers, high-temperature liquid transport containers and fishery and fish farming tanks.
The above formed articles further include members used for vehicular bumpers, door trims and instrument panels, food processing apparatuses, cooking devices, water- and oil-repellent glasses, illumination-related apparatuses, display boards and housings of OA devices, electrically illuminated billboards, displays, liquid crystal displays, cell phones, printed circuit boards, electric and electronic components, sundry goods, dust bins, bathtubs, unit baths, ventilating fans, illumination frames and the like.
Since formed articles containing the fluorine-containing copolymer of the present disclosure are excellent in the 50° C. abrasion resistance, the low hydrogen permeation, the 75° C. high-temperature rigidity, the 140° C. tensile creep resistance and the solvent crack resistance, the formed articles can suitably be utilized for nuts, bolts, joints, packings, valves, cocks, connectors, filter housings, filter cages, flowmeters, pumps, and the like. Among these, the formed articles can suitably be utilized as piping members (particularly, valves and joints) to be used for transportation of chemical solutions and flowmeter frames having flow paths of chemical solutions in flowmeters. The piping members and the flowmeter frames of the present disclosure are excellent in the 50° C. abrasion resistance, the low hydrogen permeation, the 75° C. high-temperature rigidity, the 140° C. tensile creep resistance and the solvent crack resistance. Hence, the piping members and the flowmeter frames of the present disclosure are unlikely to be abraded and unlikely to deform even when they are subjected to loads due to initiation of the flow, suspension of the flow, and changes in amount of flow of the chemical solutions.
Formed articles containing the fluorine-containing copolymer of the present disclosure can be obtained as beautiful injection molded articles at a high injection rate by an injection molding method, and since the injection molded articles are excellent in the 50° C. abrasion resistance, the low hydrogen permeation, the 75° C. high-temperature rigidity, the 140° C. tensile creep resistance and the solvent crack resistance, the injection molded articles can suitably be utilized as members to be compressed such as gaskets and packings. The members to be compressed may be gaskets or packings. The gaskets or the packings of the present disclosure can be produced at low cost by an injection molding method, and are excellent in the 50° C. abrasion resistance, the low hydrogen permeation, the 75° C. high-temperature rigidity, the 140° C. tensile creep resistance and the solvent crack resistance.
The size and shape of the members to be compressed of the present disclosure may suitably be set according to applications, and are not limited. The shape of the members to be compressed of the present disclosure may be, for example, annular. The members to be compressed of the present disclosure may also have, in plan view, a circular shape, an elliptic shape, a corner-rounded square or the like, and may be a shape having a through hole in the central portion thereof.
It is preferable that the members to be compressed of the present disclosure are used as members for constituting non-aqueous electrolyte batteries. Since the members to be compressed of the present disclosure are unlikely to be damaged even when stresses are repeatedly loaded, and are very excellent in the sealability, the members to be compressed are especially suitable as members to be used in the state of contacting with non-aqueous electrolytes in non-aqueous electrolyte batteries. That is, the members to be compressed of the present disclosure may be ones having a liquid-contact surface with a non-aqueous electrolyte in non-aqueous electrolyte batteries.
The non-aqueous electrolyte batteries are not limited as long as being batteries having a non-aqueous electrolyte, and examples thereof include lithium ion secondary batteries and lithium ion capacitors. Members constituting the non-aqueous electrolyte batteries include sealing members and insulating members.
For the non-aqueous electrolyte, one or two or more of well-known solvents can be used such as propylene carbonate, ethylene carbonate, butylene carbonate, γ-butylolactone, 1,2-dimethoxyethane, 1,2-diethoxyethane, dimethyl carbonate, diethyl carbonate and ethyl methyl carbonate. The non-aqueous electrolyte batteries may further have an electrolyte. The electrolyte is not limited, but may be LiClO4, LiAsF6, LiPF6, LiBF4, LiCl, LiBr, CH3SO3Li, CF3SO3Li, cesium carbonate and the like.
The members to be compressed of the present disclosure can suitably be utilized, for example, as sealing members such as sealing gaskets and sealing packings, and insulating members such as insulating gaskets and insulating packings. The sealing members are members to be used for preventing leakage of a liquid or a gas, or penetration of a liquid or a gas from the outside. The insulating members are members to be used for insulating electricity. The members to be compressed of the present disclosure may also be members to be used for the purpose of both of sealing and insulation.
Since the members to be compressed of the present disclosure are unlikely to be damaged even when stresses are repeatedly loaded, and are excellent in the sealability, the members to be compressed can suitably be used as sealing members for non-aqueous electrolyte batteries and insulating members for non-aqueous electrolyte batteries. Further, the members to be compressed of the present disclosure, due to containing the above fluorine-containing copolymer, have the excellent insulating property. Therefore, in the case of using the members to be compressed of the present disclosure as insulating members, the member firmly adhere to two or more electrically conductive members and prevent short circuit over a long term.
Since a thin coating layer can be formed on a core wire having a small diameter by an extrusion forming method by using the fluorine-containing copolymer of the present disclosure, the fluorine-containing copolymer can suitably be utilized as a material for forming electric wire coatings. Coated electric wires comprising a coating layer containing the fluorine-containing copolymer of the present disclosure have almost no defects causing sparks, and thus they are excellent in electric properties.
The coated electric wire has a core wire, and the coating layer installed on the periphery of the core wire and containing the fluorine-containing copolymer of the present disclosure. For example, an extrusion formed article made by melt extruding the fluorine-containing copolymer in the present disclosure on a core wire can be made into the coating layer. The coated electric wires are suitable for LAN cables (Eathernet Cables), high-frequency transmission cables, flat cables and heat-resistant cables and the like, and particularly, for transmission cables such as LAN cables (Eathernet Cables) and high-frequency transmission cables.
As a material for the core wire, for example, a metal conductor material such as copper or aluminum can be used. The core wire is preferably one having a diameter of 0.02 to 3 mm. The diameter of the core wire is more preferably 0.04 mm or larger, still more preferably 0.05 mm or larger and especially preferably 0.1 mm or larger. The diameter of the core wire is more preferable 2 mm or smaller.
With regard to specific examples of the core wire, there may be used, for example, AWG (American Wire Gauge)-46 (solid copper wire of 40 μm in diameter), AWG-26 (solid copper wire of 404 μm in diameter), AWG-24 (solid copper wire of 510 μm in diameter), and AWG-22 (solid copper wire of 635 μm in diameter).
It is preferable that the thickness of the coating layers is 0.1 to 3.0 mm. It is also preferable that the thickness of the coating layers is 2.0 mm or smaller.
The high-frequency transmission cables include coaxial cables. The coaxial cables generally have a structure configured by laminating an inner conductor, an insulating coating layer, an outer conductor layer and a protective coating layer in order from the core part to the peripheral part. A formed article containing the fluorine-containing copolymer of the present disclosure can suitably be utilized as the insulating coating layer containing the fluorine-containing copolymer. The thickness of each layer in the above structure is not limited, but is usually: the diameter of the inner conductor is approximately 0.1 to 3 mm; the thickness of the insulating coating layer is approximately 0.3 to 3 mm; the thickness of the outer conductor layer is approximately 0.5 to 10 mm; and the thickness of the protective coating layer is approximately 0.5 to 2 mm.
Alternatively, the coating layer may be one containing cells, and is preferably one in which cells are homogeneously distributed.
The average cell size of the cells is not limited, but is, for example, preferably 60 μm or smaller, more preferably 45 μm or smaller, still more preferably 35 μm or smaller, further still more preferably 30 μm or smaller, especially preferable 25 μm or smaller and further especially preferably 23 μm or smaller. Then, the average cell size is preferably 0.1 μm or larger and more preferably 1 μm or larger. The average cell size can be determined by taking an electron microscopic image of an electric wire cross section, calculating the diameter of each cell and averaging the diameters.
The foaming ratio of the coating layer may be 20% or higher, and is more preferably 30% or higher, still more preferably 33% or higher and further still more preferably 35% or higher. The upper limit is not limited, but is, for example, 80%. The upper limit of the foaming ratio may be 60%. The foaming ratio is a value determined as ((the specific gravity of an electric wire coating material−the specific gravity of the coating layer)/(the specific gravity of the electric wire coating material)×100. The foaming ratio can suitably be regulated according to applications, for example, by regulation of the amount of a gas, described later, to be injected in an extruder, or by selection of the kind of a gas dissolving.
Alternatively, the coated electric wire may have another layer between the core wire and the coating layer, and may further have another layer (outer layer) on the periphery of the coating layer. In the case where the coating layer contains cells, the electric wire of the present disclosure may be of a two-layer structure (skin-foam) in which a non-foaming layer is inserted between the core wire and the coating layer, a two-layer structure (foam-skin) in which a non-foaming layer is coated as the outer layer, or a three-layer structure (skin-foam-skin) in which a non-foaming layer is coated as the outer layer of the skin-foam structure. The non-foaming layer is not limited, and may be a resin layer composed of a resin, such as a TFE/HFP-based copolymer, a TFE/PAVE copolymer, a TFE/ethylene-based copolymer, a vinylidene fluoride-based polymer, a polyolefin resin such as polyethylene [PE], or polyvinyl chloride [PVC].
The coated electric wire can be produced, for example, by using an extruder, heating the fluorine-containing copolymer, extruding the fluorine-containing copolymer in a melt state on the core wire to thereby form the coating layer.
In formation of a coating layer, by heating the fluorine-containing copolymer and introducing a gas in the fluorine-containing copolymer in a melt state, the coating layer containing cells can be formed. As the gas, there can be used, for example, a gas such as chlorodifluoromethane, nitrogen or carbon dioxide, or a mixture thereof. The gas may be introduced as a pressurized gas in the heated fluorine-containing copolymer, or may be generated by mingling a chemical foaming agent in the fluorine-containing copolymer. The gas dissolves in the fluorine-containing copolymer in a melt state.
Then, the fluorine-containing copolymer of the present disclosure can suitably be utilized as a material for products for high-frequency signal transmission.
The products for high-frequency signal transmission are not limited as long as being products to be used for transmission of high-frequency signals, and include (1) formed boards such as insulating boards for high-frequency circuits, insulating materials for connection parts and printed circuit boards, (2) formed articles such as bases of high-frequency vacuum tubes and antenna covers, and (3) coated electric wires such as coaxial cables and LAN cables. The products for high-frequency signal transmission can suitably be used in devices utilizing microwaves, particularly microwaves of 3 to 30 GHz, in satellite communication devices, cell phone base stations, and the like.
In the products for high-frequency signal transmission, the fluorine-containing copolymer of the present disclosure can suitably be used as insulators in that the dielectric loss tangent is low.
As the (1) formed boards, printed wiring boards are preferable in that the good electric property is provided. The printed wiring boards are not limited, but examples thereof include printed wiring boards of electronic circuits for cell phones, various computers, communication devices and the like. As the (2) formed articles, antenna covers are preferable in that the dielectric loss is low.
The fluorine-containing copolymer of the present disclosure can be formed at a high forming rate into thin films uniform in thickness, and further since the obtained formed articles are excellent in the 50° C. abrasion resistance, the low hydrogen permeation, the 75° C. high-temperature rigidity, the 140° C. tensile creep resistance and the solvent crack resistance, the formed articles can suitably be utilized for films.
The films of the present disclosure are useful as release films. The release films can be produced by forming the fluorine-containing copolymer of the present disclosure by melt extrusion, calendering, press molding, casting or the like. From the viewpoint that uniform thin films can be obtained, the release films can be produced by melt extrusion.
The films of the present disclosure can be applied to roll surfaces used in QA devices. Then, the fluorine-containing copolymer of the present disclosure is formed into needed shapes by extrusion forming, compression molding, press molding or the like to be formed into sheet-shapes, filmy shapes or tubular shapes, and can be used as surface materials for QA device rolls, QA device belts or the like. Thin-wall tubes and films can be produced particularly by a melt extrusion forming method.
By molding the fluorine-containing copolymer of the present disclosure at a high injection rate by an injection molding method, beautiful injection molded articles can be obtained, and further, the obtained molded articles are excellent in 50° C. abrasion resistance, low hydrogen permeation, 75° C. high-temperature rigidity, 140° C. tensile creep resistance and solvent crack resistance; and hence the fluorine-containing copolymer can suitably be utilized for valves. Accordingly, the valves containing the fluorine-containing copolymer of the present disclosure can be produced at low cost and moreover at a high productivity, and are unlikely to be damaged even when opening and closing are repeated at a high frequency, and are excellent in the sealability. In the valves of the present disclosure, at least liquid-contact portions can be constituted of the above fluorine-containing copolymer. Further, the valves of the present disclosure may be ones having a housing containing the above fluorine-containing copolymer.
So far, embodiments have been described, but it is to be understood that various changes and modifications of patterns and details may be made without departing from the subject matter and the scope of the claims.
According to the present disclosure, there is provided a fluorine-containing copolymer comprising tetrafluoroethylene unit, hexafluoropropylene unit and perfluoro(propyl vinyl ether) unit, wherein the copolymer has a content of hexafluoropropylene unit of 7.0 to 8.5% by mass with respect to the whole of the monomer units, a content of perfluoro(propyl vinyl ether) unit of 1.5 to 2.9% by mass with respect to the whole of the monomer units, and a melt flow rate at 372° C. of 9 to 15 g/10 min.
It is preferable that the content of hexafluoropropylene unit is 7.2 to 8.1% by mass with respect to the whole of the monomer units.
It is preferable that the content of perfluoro(propyl vinyl ether) unit is 1.7 to 2.2% by mass with respect to the whole of the monomer units.
It is preferable that the melt flow rate at 372° C. is 10 to 14 g/10 min.
It is preferable that the number of functional groups is 90 or less per 106 main-chain carbon atoms.
Then, according to the present disclosure, there is provided an injection molded article comprising the above fluorine-containing copolymer.
Further, according to the present disclosure, there is provided a coated electric wire comprising a coating layer comprising the above fluorine-containing copolymer.
Further according to the present disclosure, there is provided a formed article comprising the above fluorine-containing copolymer, wherein the formed article is a valve, a joint, a flowmeter, an electric wire coating or a film.
The embodiments of the present disclosure will be described by Examples as follows, but the present disclosure is not limited only to these Examples.
Each numerical value in Examples was measured by the following methods.
(Contents of Monomer Units)
The content of each monomer unit of the fluorine-containing copolymer was measured by an NMR analyzer (for example, manufactured by Bruker BioSpin GmbH, AVANCE 300, high-temperature probe), or an infrared absorption spectrometer (manufactured by PerkinElmer, Inc., Spectrum One).
(The Number of —CF2H)
The number of —CF2H groups of the fluorine-containing copolymer was determined from a peak integrated value of the —CF2H group acquired in a 19F-NMR measurement using a nuclear magnetic resonance spectrometer AVANCE-300 (manufactured by Bruker BioSpin GmbH) and set at a measurement temperature of (the melting point of the polymer+20)° C.
(The Numbers of —COOH, —COOCH3, —CH2OH, —COF, —CF═CF2 and —CONH2)
A dried powder or pellets obtained in each of Examples and Comparative Examples were molded by cold press to prepare a film of 0.25 to 0.3 mm in thickness. The film was 40 times scanned by a Fourier transform infrared spectrometer [FT-IR (Spectrum One, manufactured by PerkinElmer, Inc.)] and analyzed to obtain an infrared absorption spectrum. The obtained infrared absorption spectrum was compared with an infrared absorption spectrum of an already known film to determine the kinds of terminal groups. Further, from an absorption peak of a specific functional group emerging in a difference spectrum between the obtained infrared absorption spectrum and the infrared absorption spectrum of the already known film, the number N of the functional group per 1×106 carbon atoms in the sample was calculated according to the following formula (A).
N=I×K/t (A)
Regarding the functional groups in Examples, for reference, the absorption frequency, the molar absorption coefficient and the correction factor are shown in Table 2. Further, the molar absorption coefficients are those determined from FT-IR measurement data of low molecular model compounds.
[Table 2]
(Melt Flow Rate (MFR))
The MFR of the fluorine-containing copolymer was determined by using a Melt Indexer G-01 (manufactured by Toyo Seiki Seisaku-sho, Ltd.), and making the polymer to flow out from a die of 2 mm in inner diameter and 8 mm in length at 372° C. under a load of 5 kg and measuring the mass (g/10 min) of the polymer flowing out per 10 min from the die, according to ASTM D1238.
(Melting Point)
The fluorine-containing copolymer was heated, as a first temperature raising step at a temperature-increasing rate of 10° C./min from 200° C. to 350° C., then cooled at a cooling rate of 10° C./min from 350° C. to 200° C., and then again heated, as second temperature raising step, at a temperature-increasing rate of 10° C./min from 200° C. to 350° C. by using a differential scanning calorimeter (trade name: X-DSC7000, manufactured by Hitachi High-Tech Science Corp.); and the melting point of the fluorine-containing copolymer was determined from a melting curve peak observed in the second temperature raising step.
40.25 kg of deionized water and 0.423 kg of methanol were fed in a 174 L-volume autoclave with a stirrer, and the autoclave inside was sufficiently vacuumized and replaced with nitrogen. Thereafter, the autoclave inside was vacuum deaerated, and in the autoclave put in a vacuum state, 40.25 kg of HFP and 1.17 kg of PPVE were fed; and the autoclave was heated to 25.5° C. Then, TFE was fed until the internal pressure of the autoclave became 0.892 MPa; and then, 1.25 kg of a 8-mass % di(ω-hydroperfluorohexanoyl) peroxide solution (hereinafter, abbreviated to DHP) was fed in the autoclave to initiate polymerization. The internal pressure of the autoclave at the initiation of the polymerization was set at 0.892 MPa, and by continuously adding TFE, the set pressure was made to be held. After 1.5 hours from the polymerization initiation, 0.423 kg of methanol was additionally fed. After 2 hours and 4 hours from the polymerization initiation, 1.25 kg of DHP was additionally fed, and the internal pressure was lowered by 0.002 MPa, respectively; after 6 hours therefrom, 0.96 kg thereof was fed and the internal pressure was lowered by 0.002 MPa. Hereafter, 0.25 kg of DHP was fed at every 2 hours until the reaction finished, and at the every time, the internal pressure was lowered by 0.002 MPa.
Then, at each time point when the amount of TFE continuously additionally fed reached 8.1 kg, 16.2 kg and 24.3 kg, 0.24 kg of PPVE was additionally fed. Then, at each time point when the amount of TFE additionally fed reached 6.0 kg and 18.1 kg, 0.423 kg of methanol was additionally fed in the autoclave. Then, when the amount of TFE additionally fed reached 40.25 kg, the polymerization was made to finish. After the finish of the polymerization, unreacted TFE and HFP were discharged to thereby obtain a wet powder. Then, the wet powder was washed with pure water, and thereafter dried at 150° C. for 10 hours to thereby obtain 44.9 kg of a dry powder.
The obtained powder was melt extruded at 370° C. by a screw extruder (trade name: PCM46, manufactured by Ikegai Corp.) to thereby obtain pellets of a copolymer. By using the obtained pellets, the above physical properties were measured by the methods described above. The results are shown in Table 3.
Copolymer pellets were obtained as in Example 1, except for changing the amount of methanol fed before the polymerization initiation to 0.354 kg, changing the each amount of methanol dividedly additionally fed after the polymerization initiation to 0.354 kg, changing the amount of PPVE fed before the polymerization initiation to 1.01 kg, changing the each amount of PPVE dividedly additionally fed after the polymerization initiation to 0.22 kg, and changing the each set pressure in the autoclave inside before and after the polymerization initiation to 0.878 MPa. By using the obtained pellets, the content of HFP and the content of PPVE were measured by the methods described above. The results are shown in Table 3.
The obtained pellets were deaerated at 200° C. for 8 hours in an electric furnace, put in a vacuum vibration-type reactor VVD-30 (manufactured by Okawara Mfg. Co. Ltd.), and heated to 200° C. After vacuumizing, F2 gas diluted to 20% by volume with N2 gas was introduced to the atmospheric pressure. 0.5 hour after the F2 gas introduction, vacuumizing was once carried out and F2 gas was again introduced. Further, 0.5 hour thereafter, vacuumizing was again carried out and F2 gas was again introduced. Thereafter, while the above operation of the F2 gas introduction and the vacuumizing was carried out once every 1 hour, the reaction was carried out at a temperature of 200° C. for 8 hours. After the reaction was finished, the reactor interior was replaced sufficiently by N2 gas to finish the fluorination reaction, thereby obtaining pellets. By using the obtained pellets, the above physical properties were measured by the methods described above. The results are shown in Table 3.
Copolymer pellets were obtained as in Example 1, except for changing the amount of methanol fed before the polymerization initiation to 0.335 kg, changing the each amount of methanol dividedly additionally fed after the polymerization initiation to 0.335 kg, changing the amount of PPVE fed before the polymerization initiation to 0.82 kg, changing the each amount of PPVE dividedly additionally fed after the polymerization initiation to 0.19 kg, and changing the each set pressure in the autoclave inside before and after the polymerization initiation to 0.866 MPa. By using the obtained pellets, the above physical properties were measured by the methods described above. The results are shown in Table 3.
Copolymer pellets were obtained as in Example 1, except for changing the amount of methanol fed before the polymerization initiation to 0.368 kg, changing the each amount of methanol dividedly additionally fed after the polymerization initiation to 0.368 kg, changing the amount of PPVE fed before the polymerization initiation to 0.99 kg, changing the each amount of PPVE dividedly additionally fed after the polymerization initiation to 0.21 kg, and changing the each set pressure in the autoclave inside before and after the polymerization initiation to 0.886 MPa. By using the obtained pellets, the content of HFP and the content of PPVE were measured by the methods described above. The results are shown in Table 3.
The obtained pellets were deaerated at 200° C. for 72 hours in an electric furnace, thereafter put in a vacuum vibration-type reactor VVD-30 (manufactured by Okawara Mfg. Co. Ltd.), and heated to 110° C. After vacuumizing, an F2 gas diluted to 20% by volume with N2 gas was introduced to the atmospheric pressure. After 0.5 hour from the F2 gas introduction, vacuumizing was once carried out and the F2 gas was again introduced. Further after 0.5 hour therefrom, vacuumizing was again carried out, and the F2 gas was again introduced. Hereafter, the F2 gas introduction and the vacuumizing operation were repeated once an hour while the reaction was carried out at a temperature of 110° C. for 8 hours. After the finish of the reaction, the reactor inside was replaced sufficiently with N2 gas to finish the fluorination reaction to thereby obtain pellets. By using the obtained pellets, the above physical properties were measured by the methods described above. The results are shown in Table 3.
Copolymer pellets were obtained as in Example 1, except for changing the amount of methanol fed before the polymerization initiation to 0.235 kg, changing the each amount of methanol dividedly additionally fed after the polymerization initiation to 0.235 kg, changing the amount of PPVE fed before the polymerization initiation to 0.96 kg, changing the each amount of PPVE dividedly additionally fed after the polymerization initiation to 0.22 kg, and changing the each set pressure in the autoclave inside before and after the polymerization initiation to 0.866 MPa. By using the obtained pellets, the HFP content and the PPVE content were measured by the methods described above. The results are shown in Table 3.
The obtained pellets were fluorinated as in Example 4. By using obtained pellets, the above physical properties were measured by the methods described above. The results are shown in Table 3.
Copolymer pellets were obtained as in Example 1, except for changing the amount of methanol fed before the polymerization initiation to 0.276 kg, changing the each amount of methanol dividedly additionally fed after the polymerization initiation to 0.276 kg, changing the amount of PPVE fed before the polymerization initiation to 0.88 kg, changing the each amount of PPVE dividedly additionally fed after the polymerization initiation to 0.22 kg, and changing the each set pressure in the autoclave inside before and after the polymerization initiation to 0.843 MPa. By using the obtained pellets, the above physical properties were measured by the methods described above. The results are shown in Table 3.
Copolymer pellets were obtained as in Example 1, except for changing the amount of methanol fed before the polymerization initiation to 0.546 kg, changing the each amount of methanol dividedly additionally fed after the polymerization initiation to 0.546 kg, changing the amount of PPVE fed before the polymerization initiation to 0.73 kg, changing the each amount of PPVE dividedly additionally fed after the polymerization initiation to 0.14 kg, and changing the each set pressure in the autoclave inside before and after the polymerization initiation to 0.906 MPa. By using the obtained pellets, the above physical properties were measured by the methods described above. The results are shown in Table 3.
0.945 kg of deionized water and 0.012 kg of methanol were fed in a 4 L-volume autoclave with a stirrer, and the autoclave inside was sufficiently vacuumized and replaced with nitrogen. Thereafter, the autoclave inside was vacuum deaerated, and in the autoclave put in a vacuum state, 0.945 kg of HFP was fed; and the autoclave was heated to 25.5° C. Then, TFE was fed until the internal pressure of the autoclave became 0.878 MPa; and then, 0.029 kg of an 8-mass % di(ω-hydroperfluorohexanoyl) peroxide solution (hereinafter, abbreviated to DHP) was fed in the autoclave to initiate polymerization. The internal pressure of the autoclave at the initiation of the polymerization was set at 0.878 MPa, and by continuously adding TFE, the set pressure was held. After 1.5 hours from the polymerization initiation, 0.012 kg of methanol was additionally fed. After 2 hours and 4 hours from the polymerization initiation, 0.029 kg of DHP was additionally fed, and the internal pressure was lowered by 0.002 MPa, respectively; after 6 hours therefrom, 0.022 kg thereof was fed and the internal pressure was lowered by 0.002 MPa. Then, at the time point when the amount of TFE additionally fed reached 0.141 kg, 0.012 kg of methanol was additionally fed in the autoclave. Then, when the amount of TFE additionally fed reached 0.473 kg, the polymerization was made to finish. After the finish of the polymerization, unreacted TFE and HFP were discharged to thereby obtain a wet powder. Then, the wet powder was washed with pure water, and thereafter dried at 150° C. for 10 hours to thereby obtain 0.518 kg of a dry powder.
The obtained powder was melt extruded at 370° C. by a 144 screw extruder (manufactured by Imoto Machinery Co. Ltd.) to thereby obtain pellets of a copolymer. By using the obtained pellets, the above physical properties were measured by the methods described above. The results are shown in Table 3.
Copolymer pellets were obtained as in Example 1, except for changing the amount of methanol fed before the polymerization initiation to 0.570 kg, changing the each amount of methanol dividedly additionally fed after the polymerization initiation to 0.570 kg, changing the amount of PPVE fed before the polymerization initiation to 1.09 kg, changing the each amount of PPVE dividedly additionally fed after the polymerization initiation to 0.19 kg, and changing the each set pressure in the autoclave inside before and after the polymerization initiation to 0.948 MPa. By using the obtained pellets, the HFP content and the PPVE content were measured by the methods described above. The results are shown in Table 3.
The obtained pellets were fluorinated as in Example 2. By using the obtained pellets, the above physical properties were measured by the methods described above. The results are shown in Table 3.
Copolymer pellets were obtained as in Example 1, except for changing the amount of methanol fed before the polymerization initiation to 0.411 kg, changing the each amount of methanol dividedly additionally fed after the polymerization initiation to 0.411 kg, changing the amount of PPVE fed before the polymerization initiation to 0.96 kg, changing the each amount of PPVE dividedly additionally fed after the polymerization initiation to 0.22 kg, and changing the each set pressure in the autoclave inside before and after the polymerization initiation to 0.866 MPa. By using the obtained pellets, the HFP content and the PPVE content were measured by the methods described above. The results are shown in Table 3.
The obtained pellets were fluorinated as in Example 2. By using the obtained pellets, the above physical properties were measured by the methods described above. The results are shown in Table 3.
945 g of deionized water and 7.7 g of methanol were fed in a 4 L-volume autoclave with a stirrer, and the autoclave inside was sufficiently vacuumized and replaced with nitrogen. Thereafter, the autoclave inside was vacuum deaerated, and in the autoclave put in a vacuum state, 945 g of HFP and 23.6 g of PEVE were fed; and the autoclave was heated to 25.5° C. Then, TFE was fed until the internal pressure of the autoclave became 0.881 MPa; and then, 29.4 g of an 8-mass % di(ω-hydroperfluorohexanoyl) peroxide solution (hereinafter, abbreviated to DHP) was fed in the autoclave to initiate polymerization. The internal pressure of the autoclave at the initiation of the polymerization was set at 0.881 MPa, and by continuously adding TFE, the set pressure was held. After 1.5 hours from the polymerization initiation, 7.7 g of methanol was additionally fed. After 2 hours and 4 hours from the polymerization initiation, 29.4 g of DHP was additionally fed, and the internal pressure was lowered by 0.002 MPa, respectively; after 6 hours therefrom, 22.6 g thereof was fed and the internal pressure was lowered by 0.002 MPa. Hereafter, 6.0 g of DHP was additionally fed at every 2 hours until the reaction finished, and at the every time, the internal pressure was lowered by 0.002 MPa.
Then, at each time point when the amount of TFE continuously additionally fed reached 190 g and 380 g, 5.2 g of PEVE was additionally fed. Then, when the amount of TFE additionally fed reached 140 g, 7.8 g of methanol was additionally fed in the autoclave. Then, when the amount of TFE additionally fed reached 454 g, the polymerization was made to finish. After the finish of the polymerization, unreacted TFE and HFP were discharged to thereby obtain a wet powder. Then, the wet powder was washed with pure water, and thereafter dried at 150° C. for 10 hours to thereby obtain 509 g of a dry powder.
The obtained powder was melt extruded at 370° C. by a 144 screw extruder (manufactured by Imoto Machinery Co. Ltd.) to thereby obtain pellets of a copolymer. By using the obtained pellets, the HFP content and the PEVE content were measured by the methods described above. The results are shown in Table 3.
The obtained pellets were deaerated at 200° C. for 8 hours in an electric furnace, thereafter put in a portable reactor TVS-1 type (manufactured by Taiatsu Glass Industry Inc.), and heated to 200° C. After vacuumizing, an F2 gas diluted to 20% by volume with N2 gas was introduced to the atmospheric pressure. After 0.5 hour from the F2 gas introduction, vacuumizing was once carried out and the F2 gas was again introduced. Further after 0.5 hour therefrom, vacuumizing was again carried out, and the F2 gas was again introduced. Hereafter, the F2 gas introduction and the vacuumizing operation were repeated once an hour while the reaction was carried out at a temperature of 200° C. for 8 hours. After the finish of the reaction, the reactor inside was replaced sufficiently with N2 gas to finish the fluorination reaction to thereby obtain pellets. By using the obtained pellets, the above physical properties were measured by the methods described above. The results are shown in Table 3.
The description of “<9” in Table 3 means that the number of —CF2H groups was less than 9. The description of “<6” in Table 3 means that the total number (number of functional groups, N) of —COOH, —COOCH3, —CH2OH, —COF, —CF═CF2 and —CONH2 was less than 6.
Then, by using the obtained pellets, the following properties were evaluated. The results are shown in Table 4.
(Abrasion Test)
By using the pellets and a heat press molding machine, a sheet-shape test piece of approximately 0.2 mm in thickness was prepared and cut out into a test piece of 10 cm×10 cm. The prepared test piece was fixed on a test bench of a Taber abrasion tester (No. 101, Taber type abrasion tester with an option, manufactured by Yasuda Seiki Seisakusho, Ltd.), and the abrasion test was carried out under the conditions of at a test piece surface temperature of 50° C., at a load of 500 g, using an abrasion wheel CS-10 (rotationally polished in 20 rotations with an abrasion paper #240), and at a rotation rate of 60 rpm, using the Taber abrasion tester. The weight of the test piece after 1,000 rotations was measured, and the same test piece was further subjected to the test of 7,000 rotations and thereafter, the weight thereof was measured. The abrasion loss was determined by the following formula.
Abrasion loss (mg)=M1−M2
(Hydrogen Permeation Coefficient)
By using the pellets and a heat press molding machine, a sheet-shape test piece of approximately 0.1 mm in thickness was prepared. Measurement of the hydrogen permeability was carried out on the obtained test piece according to a method described in JIS K7126-1:2006 by using a differential pressure type permeability tester (L100-5000 type gas permeability tester, manufactured by Systech illinois Ltd.). There was obtained a numerical value of the hydrogen permeability at a permeation area of 50.24 cm2, a test temperature of 60° C. and at a test humidity of 0% RH. By using the obtained hydrogen permeability and the thickness of the test piece, the hydrogen permeability coefficient was calculated by the following formula.
hydrogen permeability coefficient (cm3·mm/(m2·24h·atm))=GTR×d
(75° C. Load Deflection Rate)
By using the pellets and a heat press molding machine, a sheet-shape test piece of approximately 2.4 mm in thickness was prepared and cut out into a test piece of 80×10 mm; and the test piece was heated in an electric furnace at 100° C. for 20 hours. A test for the 85° C. load deflection rate was carried out according to a method described in JIS K7191-1 except for using the obtained test piece, by a heat distortion tester (manufactured by Yasuda Seiki Seisakusho, Ltd.) under the conditions of at a test temperature of 30 to 150° C., at a temperature-increasing rate of 120° C./h, at a bending stress of 1.8 MPa and the flatwise method. The load deflection rate was determined by the following formula. A sheet low in the 75° C. load deflection rate is excellent in the 75° C. high-temperature rigidity.
Load deflection rate (%)=a2/a1×100
(Tensile Creep Test)
The tensile creep strain was measured by using TMA-7100, manufactured by Hitachi High-Tech Science Corp. By using the pellets and a heat press molding machine, a sheet of approximately 0.1 mm in thickness was prepared, and a sample of 2 mm in width and 22 mm in length was prepared from the sheet. The sample was mounted on measurement jigs with the distance between the jigs of 10 mm. A load was applied on the sample so that the cross-sectional load became 3.32 N/mm2, and allowed to stand at 140° C.; and there was measured the displacement (mm) from the timepoint of 90 min from the test initiation to the timepoint of 450 min from the test initiation, and there was calculated the proportion (tensile creep strain (%)) of the displacement (mm) to the initial sample length (10 mm). A sheet low in the tensile creep stain (%) measured under the condition of at 140° C. for 450 min is hardly elongated even when a tensile load is applied for a long time in a high-temperature environment, being excellent in the high-temperature tensile creep property (140° C.).
(Chemical Solution Immersion Crack Test)
By using the pellets and a heat press molding machine, a formed article of approximately 2 mm in thickness was prepared. The obtained sheet was punched out by using a rectangular dumbbell of 13.5 mm×38 mm to obtain three test pieces. A notch was formed on the middle of a long side of the each obtained test piece by a blade of 19 mm×0.45 mm according to ASTM D1693. The three notched test pieces and 25 g of N-methylpyrollidone were put in a 100-mL polypropylene-made bottle and heated in an electric furnace at 150° C. for 20 hours; thereafter, the notched test pieces were taken out. The obtained three notched test pieces were mounted on a stress crack test jig according to ASTM D1693, and heated in an electric furnace at 150° C. for 24 hours; thereafter, the notches and their vicinities were visually observed and the number of cracks was counted. A sheet having no crack generated is excellent in the solvent crack resistance.
(Injection Moldability)
The copolymer was injection molded by using an injection molding machine (SE50EV-A, manufactured by Sumitomo Heavy Industries, Ltd.) set at a cylinder temperature of 385° C., a metal mold temperature of 180° C. and an injection speed of 20 mm/s. The metal mold used was a metal mold (100 mm×100 mm×2.0 mmt, film gate, flow length from the gate: 100 mm) Cr plated on HPM38. The obtained injection molded article was observed and evaluated according to the following criteria. The presence/absence of white turbidness was visually checked. The presence/absence of roughness of the surface was checked by touching the surface of the injection molded article.
(Electric Wire Coating Extrusion Conditions)
By using a 30-mmϕ electric wire coating extruder (manufactured by Tanabe Plastics Machinery Co. Ltd.), the fluorine-containing copolymer was extrusion coated in the following coating thickness on a copper conductor of 0.50 mm in conductor diameter to thereby obtain a coated electric wire. The electric wire coating extrusion conditions were as follows.
(Coating Shortage)
Electric wire coating extrusion was continuously carried out; and the case where coating shortage occurred once or more times in one hour was taken as impassable in continuous extrusion (Poor), and the case where no coating shortage occurred was taken as passable in continuous extrusion (Good).
(Spark)
A spark tester (DENSOK HIGH FREQ SPARK TESTER) was installed online on an electric wire coating line, and the presence/absence of defects of the electric wire coating was evaluated at a voltage of 1,500 V. One-hour continuous extrusion was carried out and the number of sparks was counted.
(Film Moldability)
By using a ϕ14-mm extruder (manufactured by Imoto Machinery Co. Ltd.) and a T die, the pellets were formed to prepare a film. The extrusion conditions were as follows.
The extrusion forming of the fluorine-containing copolymer was continued until the fluorine-containing copolymer became enabled to be stably extruded from the extruder. Successively, by extruding the fluorine-containing copolymer, a film (70 mm wide) of 11 m or longer in length was prepared so that that thickness became 0.10 mm. A portion of 10 to 11 m of the obtained film was cut out from one end of the film and there was prepared a test piece (1 m long and 70 mm wide) for measuring the fluctuation in the thickness. Then, there were measured thicknesses of 3 points in total on one end of the obtained film of a middle point in the width direction and 2 points separated by 25 mm from the middle point in the width direction. Further, there were measured 9 points in total of 3 middle points in the width direction spaced at intervals of 25 cm from the middle point in the width direction of the one end of the film toward the other end thereof, and 2 points separated by 25 mm in the width direction from the each middle point of the 3 middle points. Among the 12 measurement values in total, the case where the number of points having measurement values out of the range of ±10% of 0.10 mm was 1 or less was taken as good; and the case where the number of points having measurement values out of the range of ±10% of 0.10 mm was 2 or more was taken as poor.
(Immersion Test in a Hydrogen Peroxide Aqueous Solution)
By using the pellets and a heat press molding machine, a sheet of approximately 0.2 mm in thickness was prepared and test pieces of 15 mm square were prepared. 10 sheets of the test pieces and 15 g of a 3-mass % hydrogen peroxide aqueous solution were put in a 50-mL polypropylene-made bottle, and heated in an electric furnace at 95° C. for 20 hours, and thereafter cooled to room temperature. The test pieces were removed from the hydrogen peroxide aqueous solution; and a TISAB solution (10) (manufactured by Kanto Chemical Co., Inc.) was added to the remaining hydrogen peroxide aqueous solution; and the fluorine ion concentration in the obtained hydrogen peroxide aqueous solution was measured by a fluorine ion meter. The fluorine ion concentration (concentration of fluorine ions having dissolved out) per sheet weight was calculated from an obtained measurement value according to the following formula.
Dissolving-out fluorine ion concentration (ppm by mass)=the measurement value (ppm×the amount of the hydrogen peroxide aqueous solution (g)/the weight of the test piece (g)
| Number | Date | Country | Kind |
|---|---|---|---|
| 2021-031099 | Feb 2021 | JP | national |
This application is a Rule 53(b) Continuation of International Application No. PCT/JP2022/008438 filed Feb. 28, 2022, which claims priority based on Japanese Patent Application No. 2021-031099 filed Feb. 26, 2021, the respective disclosures of which are incorporated herein by reference in their entirety.
| Number | Date | Country | |
|---|---|---|---|
| Parent | PCT/JP2022/008438 | Feb 2022 | US |
| Child | 18452878 | US |
