WO2023249053A1 - Method for producing film - Google Patents

Method for producing film Download PDF

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Publication number
WO2023249053A1
WO2023249053A1 PCT/JP2023/022937 JP2023022937W WO2023249053A1 WO 2023249053 A1 WO2023249053 A1 WO 2023249053A1 JP 2023022937 W JP2023022937 W JP 2023022937W WO 2023249053 A1 WO2023249053 A1 WO 2023249053A1
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WIPO (PCT)
Prior art keywords
film
heat treatment
hot air
bis
acid
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PCT/JP2023/022937
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French (fr)
Japanese (ja)
Inventor
伝一朗 水口
治美 米虫
洋行 涌井
幸太 北村
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東洋紡株式会社
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Publication of WO2023249053A1 publication Critical patent/WO2023249053A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B13/00Conditioning or physical treatment of the material to be shaped
    • B29B13/02Conditioning or physical treatment of the material to be shaped by heating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/02Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
    • B29C55/04Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets uniaxial, e.g. oblique
    • B29C55/08Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets uniaxial, e.g. oblique transverse to the direction of feed
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F1/00Compounds containing elements of Groups 1 or 11 of the Periodic Table
    • C07F1/10Silver compounds

Definitions

  • the present invention relates to a method for producing a film.
  • a tenter-type conveying device that conveys the object in a state in which the object is held (see, for example, Patent Document 1).
  • the pin tenter conveyance device grips the film by piercing both ends of the film with a large number of pins along the flow direction. It has a large number of pins arranged on the sheet. The pin grips and transports the film, but if the tear strength of the film is low, it may break during transport.
  • both ends of the film are broken or torn in this way, the film being transported will come off the pin gripping portion, and the film will remain in the transport device, making it impossible to obtain the desired film. Furthermore, even if such accumulation in the conveying device does not occur, tearing or breaking at both ends of the film makes it difficult to maintain the proper tension of the film, and as a result, wrinkles occur throughout the film, causing damage to the edges. It can also be a cause of other quality deterioration. Furthermore, if tearing or abnormal appearance occurs near both ends of the film, it becomes necessary to cut more to the center when cutting the gripping portion, causing production loss.
  • the present invention has been made in view of the above-mentioned problems, and its purpose is to prevent breakage, tearing, and appearance abnormalities at both ends of the film and the vicinity thereof when the film is transported with both ends fixed by a tenter-type transport device. It is an object of the present invention to provide a method for producing a film that can more effectively suppress the occurrence of the problem.
  • the present inventors have completed the present invention as a result of intensive studies to solve the above problems. That is, the present invention provides the following preferred embodiments.
  • a method for producing a film comprising: Step A of installing fixtures at both ends in the width direction of one side of the film before heat treatment, and fixing the heat treated film with the fixtures; Step B of blowing hot air onto both sides of the film before heat treatment Step C of conveying the film before heat treatment has
  • the process B is characterized in that the speed of the hot air blown to the surface where the fixing device is not installed is the same as or higher than the speed of the hot air blown to the surface where the fixing device is installed.
  • Production method. [2] The method for producing a film according to [1], wherein in the step B, the wind speed on the surface where the fixing device is not installed is 1.1 times or more the wind speed on the surface where the fixing device is installed. .
  • Blowing mechanism B blowing hot air to both sides of the film before heat treatment
  • Conveyance mechanism C that conveys the film before heat treatment has
  • the blowing mechanism B is a film characterized in that the speed of the hot air blown to the surface where the fixing device is not installed is the same as or higher than the speed of the hot air blown to the surface where the fixing device is installed.
  • manufacturing equipment [7] The production of the film according to [6], wherein the air blowing mechanism B has a wind speed on a surface where the fixing device is not installed is 1.1 times or more as a wind speed on the surface where the fixing device is installed. Device. [8] The film manufacturing apparatus according to [6] or [7], wherein the fixture is a pin sheet. [9] The film manufacturing apparatus according to any one of [6] to [8], wherein the film is a polyimide film. [10] The film manufacturing apparatus according to [9], wherein the polyimide film is a transparent polyimide film.
  • the present invention it is possible to provide a method for manufacturing a film that does not cause breakage, tearing, or abnormal appearance not only at the center of the film but also at and around both ends where the film is fixed.
  • film transport defects caused by breakage and tearing of both ends of the film can be suppressed. Furthermore, wrinkles in the center caused by abnormalities at both ends can be suppressed, and a film of stable quality can be provided. Furthermore, since breakage, tearing, and abnormal appearance near both ends of the film can be suppressed, both ends to be cut can be made smaller, and production loss can be reduced. Furthermore, by using the method of the present invention, excessive heat is not applied to the center of the film, so a film of stable quality can be provided without causing abnormalities in the center of the film.
  • FIGS. 1 and 2 An explanatory diagram schematically showing the state of the film during transport of the present invention An explanatory diagram schematically showing another state of the film during conveyance according to the present invention.
  • the hot air is not blown out from three points each at the top and bottom, but is blown out evenly from the entire width direction of the air outlet. ing.
  • a plurality of air outlets are arranged in the film transport direction.
  • the film before heat treatment may be passed through a heating furnace to volatilize organic solvents, cause chemical reactions, and improve various physical properties.
  • the film for the purpose of volatilizing the organic solvent is the film before drying
  • the film for the purpose of causing a chemical reaction is the precursor film (green film), but in this specification, these are collectively referred to as the film before heat treatment. That's what it means.
  • the fixing method is not particularly limited.
  • a tenter-type transportation device is generally used.
  • the film before heat treatment is fixed only at both ends. By fixing only at both ends, air blowing at a location other than both ends (for example, the center) of the film before heat treatment is not blocked.
  • a hot air generation mechanism When heating the film before heat treatment in the tenter-type conveying device, a hot air generation mechanism is often used as the heating source.
  • the hot air generation mechanism blows hot air onto the surface of the film before heat treatment where the fixing device is not installed (e.g., the upper surface of the film before heat treatment) and the surface of the film before heat treatment where the fixer is installed (e.g., the lower surface of the film before heat treatment). and heat it (Step B).
  • heat treatment it is possible to volatilize the organic solvent in the film before heat treatment, cause a chemical reaction, and improve various physical properties. It is necessary that the speed of the hot air on the surface of the film before heat treatment on which the fixture is not installed is equal to or higher than the speed of the hot air on the surface where the fixture is installed.
  • blowing hot air onto the film before heat treatment is also referred to as heat treatment.
  • FIG. 1 is an explanatory diagram schematically showing the state of the film before heat treatment during transportation according to the present invention.
  • the film before heat treatment is conveyed from the back side of the page to the front side (or from the front side to the back side).
  • a pin sheet 11 film fixing device
  • pins 11a film fixing structure
  • the heat treatment is performed using hot air 31 generated from a hot air outlet 21 provided on the non-fixing device installation surface side (upper surface) of the film 1 before heat treatment, and hot air 31 generated from the hot air outlet 21 provided on the non-fixing device installation surface side (lower surface) of the film 1 before heat treatment.
  • This is done by simultaneously blowing hot air 32 generated from a hot air outlet 22 from both upper and lower surfaces of the film 1 before heat treatment.
  • the hot air 31 is blown onto the pre-heat-treated film 1 without being blocked by the pin sheet 11, but a part of the hot air 32 is blocked by the pin sheet 11 and does not reach the edge 1b of the pre-heat-treated film. .
  • the hot air 32 is blown unobstructed to the central portion 1a of the film before heat treatment. Normally, this would cause the end portion 1b of the film before heat treatment to undergo an incomplete state of chemical reaction or an undried state of the solvent.
  • the total amount of hot air 31 and hot air 32 is increased in an attempt to increase the amount of hot air 31 (hot air that is not blocked by pin sheet 11) blown onto the film end 1b before heat treatment, the product may become damaged. Excessive heat is applied to the central portion 1a of the film, causing abnormalities such as clouding, yellowing, and breakage due to excessive drying.
  • hot air 32 (which is blocked by pin sheet 11)
  • the above-mentioned condition at the end portion 1b of the film before heat treatment can be avoided without causing the above-mentioned abnormality in the central portion 1a of the film.
  • the hot air outlet 21 side of the film 1 before heat treatment is the non-fixing device installation surface
  • the hot air outlet 22 side is the fixing device installation surface.
  • a pin tenter 11 is installed on the upper surface of the film before heat treatment, and both ends of the film 1 before heat treatment are fixed by piercing pins 11a provided on the lower surface of the pin sheet 11. You can.
  • the wind speed of the hot air 31 on the side of the film 1 before heat treatment where the fixing device is not installed is the same as the wind speed of the hot air 32 on the side of the film 1 before heat treatment where the fixing device is installed (the upper side). , make it larger than that.
  • the hot air outlet 22 side of the film 1 before heat treatment is the fixture installation surface
  • the hot air outlet 21 side is the fixture non-installation surface.
  • the pin tenter type conveying device generally has a large number of pins arranged on a pin sheet fixed (grasped) by a pair of moving chains arranged parallel to each other.
  • the pins arranged on this pin sheet may be on the upper surface or the lower surface of the pin sheet.
  • the arrangement of the pins is not particularly limited, and conventionally known pins can be used.
  • the temperature of the hot air blown (blown) on the non-fixing device installation surface and the fixing device installation surface of the film before heat treatment is 80° C. or higher and 500° C. or lower in order to promote solvent volatilization and chemical reactions.
  • the temperature is more preferably 120°C or higher because it is easy to remove the solvent contained in the film before heat treatment, and when the film before heat treatment is a polyimide precursor (polyamic acid), it is easy to imidize (thermal imidization). , more preferably 150°C or higher, particularly preferably 200°C or higher.
  • the temperature is more preferably 450°C or lower, still more preferably 400°C or lower, and particularly preferably 380°C or lower.
  • the hot air temperatures on the fixture-free surface and the fixture-installed surface may be the same or different, but are preferably the same temperature from the viewpoint of simplifying the apparatus. Changes in the temperature of the hot air during film transport are not particularly limited, and the design may be such that multiple heating furnaces are connected to change the temperature of the hot air in stages. It may be designed to gradually rise or fall.
  • the number of heating furnaces is preferably 2 or more and 10 or less, more preferably 3 or more and 8 or less, and even more preferably 4 or more and 6 or less.
  • the speed of the hot air blown to the surface of the film before heat treatment on which the fixing device is not installed is 0.5 m/sec or more and 15 m/sec or less.
  • the hot air sufficiently reaches the film before heat treatment, making it easier to remove the solvent contained in the film before heat treatment, and if the film before heat treatment is a polyimide precursor (polyamic acid), it becomes easier to imidize (thermal imidization). Therefore, it is more preferably 1 m/sec or more, still more preferably 1.5 m/sec or more, even more preferably 2 m/sec or more, and particularly preferably 3 m/sec or more.
  • the speed is preferably 13 m/sec or less, more preferably 12 m/sec or less, and even more preferably 10 m/sec or less, since it can suppress breakage, tearing, pin detachment, etc. due to flapping of the film before heat treatment. .
  • the speed of the hot air blown onto the fixing device installation surface of the film before heat treatment is 0.4 m/sec or more and 14 m/sec or less. More preferably 0.9 m, since it is easy to remove the solvent contained in the film before heat treatment, and when the film before heat treatment is a polyimide precursor (polyamic acid), it is easy to imidize (thermal imidization). /sec or more, more preferably 1.4 m/sec or more, even more preferably 1.9 m/sec or more.
  • the speed is preferably 12 m/sec or less, more preferably 11 m/sec or less, and even more preferably 9 m/sec or less, since it can suppress breakage, tearing, pin detachment, etc. due to flapping of the film before heat treatment. .
  • the speed of the hot air blown to the surface of the pre-heat-treated film on which the fixing device is not installed needs to be the same as or higher than the speed of the hot air blown to the surface where the fixing device is installed.
  • the ratio of wind speeds between the fixture non-installation surface and the fixture installation surface is preferably greater than 1.0. Preferably, 1. 05 or more, more preferably 1.1 or more. In addition, it is preferably 10 or less because it suppresses the temperature drop in the space on the side where the fixture is installed and the temperature drop in the film itself due to the temperature drop, making it easier to dry the entire film before heat treatment and complete the chemical reaction. , more preferably 5 or less, still more preferably 3 or less.
  • the edges of the film before heat treatment require more time to dry and complete the chemical reaction than the center of the film before heat treatment. When only the edges of the film are dry or the chemical reaction is not completed, the edges of the film do not have sufficient strength, and appearance abnormalities such as tearing and elongation may occur starting from the film fixing structure (pin 11a).
  • the residual solvent contained in the heat-treated and dried film is preferably 500 ppm or less, more preferably 200 ppm or less, and still more preferably 100 ppm or less.
  • the film of the present invention is preferably manufactured by a method in which it is wound up as a long film having a width of 300 mm or more and a length of 10 m or more. Furthermore, the method for fixing both widthwise ends of one side of the film before heat treatment is not particularly limited, and may be held by sticking it into a pin of a pin tenter-type conveyance device, or by holding it with a clip of a clip tenter-type conveyance device. It may also be gripped.
  • the width of both ends is not particularly limited as long as it can be fixed using a conventionally known tenter-type conveyance device.
  • the lower limit is preferably 5 mm or more, more preferably 10 mm or more.
  • the total width of both ends is preferably 0.1% or more of the total width of the film before heat treatment, more preferably 0.5% or more, and still more preferably 1% or more.
  • the upper limit of the width of both ends (width of each end) is preferably 100 mm or less, more preferably 50 mm or less.
  • the total width of both ends is preferably at most 50% of the total width of the film, more preferably at most 30%, even more preferably at most 10%.
  • the central part in the width direction of the film before heat treatment is preferably a position 30 to 70% from one end, more preferably 40 to 60% when the full width of the film before heat treatment is 100%.
  • the position is more preferably 45 to 55%.
  • the transport speed of the film before heat treatment can be appropriately set depending on the heat treatment conditions (hot air temperature, wind speed, etc.). Although it is difficult to determine an appropriate conveying speed strictly because it depends on the length of the heat treatment furnace, if it is slow, there is a risk that productivity will decrease. Preferably it is 0.05 m/min or more, more preferably 0.1 m/min or more.
  • the film of the present invention includes polyimide resins such as polyimide, polyamideimide, polyetherimide, and fluorinated polyimide (e.g., aromatic polyimide resin, alicyclic polyimide resin); polyolefin resins such as polyethylene and polypropylene.
  • polyimide resins such as polyimide, polyamideimide, polyetherimide, and fluorinated polyimide (e.g., aromatic polyimide resin, alicyclic polyimide resin); polyolefin resins such as polyethylene and polypropylene.
  • Copolymerized polyesters such as polyethylene terephthalate, polybutylene terephthalate, and polyethylene-2,6-naphthalate (e.g., fully aromatic polyesters, semi-aromatic polyesters); Copolymerized (meth)acrylates represented by polymethyl methacrylate; Polycarbonates; Polyamides ; polysulfone; polyethersulfone; polyetherketone; cellulose acetate; cellulose nitrate; aromatic polyamide; polyvinyl chloride; polyphenol; polyarylate; polyphenylene sulfide; polyphenylene oxide; polystyrene.
  • Copolymerized polyesters such as polyethylene terephthalate, polybutylene terephthalate, and polyethylene-2,6-naphthalate (e.g., fully aromatic polyesters, semi-aromatic polyesters); Copolymerized (meth)acrylates represented by polymethyl methacrylate; Polycarbonates; Polyamides ; polysulfone; polyether
  • the above-mentioned film is premised on being suitably used in a process involving heat treatment at 250° C. or higher, there are a limited number of polymer films that can actually be used among the exemplified polymer films.
  • Particularly preferred specific examples include aromatic polyimide film, aromatic amide film, aromatic amide-imide film, aromatic benzoxazole film, aromatic benzothiazole film, aromatic benzimidazole film, and the like.
  • the film before heat treatment of the present invention is a film containing an organic solvent in the film (pre-drying film), a film before chemical reaction (precursor film), or a precursor film containing an organic solvent (dried precursor film). ) etc.
  • the organic solvent content of the film before heat treatment is preferably 50% by mass or less, more preferably 45% by mass or less, and even more preferably 40% by mass, since both ends of the film before heat treatment can be fixed (held) and transported. % or less. Further, from the viewpoint of manufacturing efficiency and cost, the content is preferably 10% by mass or more, more preferably 15% by mass or more, and still more preferably 20% by mass or more.
  • polyimide resin films are produced by applying a polyamic acid (polyimide precursor) solution obtained by reacting diamines and tetracarboxylic acids in a solvent to a support for polyimide film production, and drying it to form a green film (hereinafter referred to as green film). (also referred to as a "polyamic acid film”), and is obtained by further heat-treating the green film at a high temperature on a support for producing a polyimide film or in a state peeled from the support to perform a dehydration ring-closing reaction.
  • This polyamic acid film is a polyimide precursor film.
  • polyamic acid polyimide precursor, hereinafter also referred to as polyamic acid
  • solution coating means such as slit die coating can be used as appropriate.
  • the diamines constituting the polyamic acid are not particularly limited, and aromatic diamines, aliphatic diamines, alicyclic diamines, etc. commonly used in polyimide synthesis can be used. From the viewpoint of heat resistance, aromatic diamines are preferred. Diamines may be used alone or in combination of two or more.
  • the diamines are not particularly limited, and include, for example, oxydianiline (bis(4-aminophenyl) ether), paraphenylenediamine (1,4-phenylenediamine), and the like.
  • Tetracarboxylic acids constituting polyamic acids include aromatic tetracarboxylic acids (including their acid anhydrides), aliphatic tetracarboxylic acids (including their acid anhydrides), and alicyclic tetracarboxylic acids that are commonly used in polyimide synthesis. Acids (including their acid anhydrides) can be used. When these are acid anhydrides, the number of anhydride structures in the molecule may be one or two, but those having two anhydride structures (dianhydride) are preferable. good. Tetracarboxylic acids may be used alone or in combination of two or more.
  • the tetracarboxylic acid is not particularly limited and includes, for example, pyrolimet dianhydride, 3,3',4,4'-biphenyltetracarboxylic dianhydride, and the like.
  • the polyimide film may be a transparent polyimide film.
  • a colorless and transparent polyimide which is an example of the film, will be explained. Hereinafter, to avoid complexity, it will also be simply referred to as transparent polyimide.
  • the total light transmittance is 75% or more. It is more preferably 80% or more, still more preferably 83% or more, even more preferably 84% or more, particularly preferably 85% or more.
  • the upper limit of the total light transmittance of the transparent polyimide is not particularly limited, but for use as a flexible electronic device, it is preferably 98% or less, more preferably 97% or less.
  • the colorless transparent polyimide in the present invention is preferably a polyimide having a total light transmittance of 75% or more.
  • Aromatic tetracarboxylic acids for obtaining colorless and highly transparent polyimide include 4,4'-(2,2-hexafluoroisopropylidene)diphthalic acid, 4,4'-oxydiphthalic acid, and bis(1,3- dioxo-1,3-dihydro-2-benzofuran-5-carboxylic acid) 1,4-phenylene, bis(1,3-dioxo-1,3-dihydro-2-benzofuran-5-yl)benzene-1,4 -dicarboxylate, 4,4'-[4,4'-(3-oxo-1,3-dihydro-2-benzofuran-1,1-diyl)bis(benzene-1,4-diyloxy)]dibenzene- 1,2-dicarboxylic acid, 3,3',4,4'-benzophenonetetracarboxylic acid, 4,4'-[(3-oxo-1,3-dihydro-2-benz
  • Examples include tetracarboxylic acids and their acid anhydrides.
  • dianhydrides having two acid anhydride structures are preferred, particularly 4,4'-(2,2-hexafluoroisopropylidene)diphthalic dianhydride, 4,4'-oxydiphthalic dianhydride, Acid dianhydrides are preferred.
  • the aromatic tetracarboxylic acids may be used alone or in combination of two or more kinds.
  • the amount of copolymerized aromatic tetracarboxylic acids is preferably 50% by mass or more of the total tetracarboxylic acids, more preferably 60% by mass or more, and still more preferably 70% by mass.
  • the content is more preferably 80% by mass or more, particularly preferably 90% by mass or more, and may be 100% by mass.
  • alicyclic tetracarboxylic acids include 1,2,3,4-cyclobutanetetracarboxylic acid, 1,2,3,4-cyclopentanetetracarboxylic acid, 1,2,3,4-cyclohexanetetracarboxylic acid, 1 , 2,4,5-cyclohexanetetracarboxylic acid, 3,3',4,4'-bicyclohexyltetracarboxylic acid, bicyclo[2,2,1]heptane-2,3,5,6-tetracarboxylic acid, Bicyclo[2,2,2]octane-2,3,5,6-tetracarboxylic acid, bicyclo[2,2,2]oct-7-ene-2,3,5,6-tetracarboxylic acid, tetrahydroanthracene -2,3,6,7-tetracarboxylic acid, tetradecahydro-1,4:5,8:9,10-trimethanoanthracene-2
  • dianhydrides having two acid anhydride structures are preferred, particularly 1,2,3,4-cyclobutanetetracarboxylic dianhydride and 1,2,3,4-cyclohexanetetracarboxylic dianhydride.
  • Acid dianhydride, 1,2,4,5-cyclohexanetetracarboxylic dianhydride is preferred, and 1,2,3,4-cyclobutanetetracarboxylic dianhydride, 1,2,4,5-cyclohexanetetracarboxylic dianhydride
  • Acid dianhydride is more preferred, and 1,2,3,4-cyclobutanetetracarboxylic dianhydride is even more preferred. Note that these may be used alone or in combination of two or more.
  • the amount of copolymerized alicyclic tetracarboxylic acids is, for example, preferably 50% by mass or more of the total tetracarboxylic acids, more preferably 60% by mass or more, and still more preferably 70% by mass. % or more, still more preferably 80% by mass or more, particularly preferably 90% by mass or more, and may even be 100% by mass.
  • tricarboxylic acids examples include aromatic tricarboxylic acids such as trimellitic acid, 1,2,5-naphthalene tricarboxylic acid, diphenyl ether-3,3',4'-tricarboxylic acid, and diphenylsulfone-3,3',4'-tricarboxylic acid.
  • acids, or hydrogenated products of the above aromatic tricarboxylic acids such as hexahydrotrimellitic acid, alkylenes such as ethylene glycol bis trimellitate, propylene glycol bis trimellitate, 1,4-butanediol bis trimellitate, and polyethylene glycol bis trimellitate.
  • examples include glycol bistrimelitate, and monoanhydrides and esterified products thereof. Among these, monoanhydrides having one acid anhydride structure are preferred, and trimellitic anhydride and hexahydrotrimellitic anhydride are particularly preferred. Incidentally, these may be used alone or in combination.
  • dicarboxylic acids examples include aromatic dicarboxylic acids such as terephthalic acid, isophthalic acid, orthophthalic acid, naphthalene dicarboxylic acid, 4,4'-oxydibenzenecarboxylic acid, or the above-mentioned aromatic dicarboxylic acids such as 1,6-cyclohexanedicarboxylic acid.
  • examples include esterified products.
  • aromatic dicarboxylic acids and hydrogenated products thereof are preferred, with terephthalic acid, 1,6-cyclohexanedicarboxylic acid, and 4,4'-oxydibenzenecarboxylic acid being particularly preferred.
  • dicarboxylic acids may be used alone or in combination.
  • Diamines or isocyanates for obtaining colorless and highly transparent polyimides are not particularly limited, and include aromatic diamines, aliphatic diamines, and alicyclic diamines commonly used in polyimide synthesis, polyamide-imide synthesis, and polyamide synthesis.
  • diisocyanates, aromatic diisocyanates, aliphatic diisocyanates, alicyclic diisocyanates, etc. can be used. From the viewpoint of heat resistance, aromatic diamines are preferred, and from the viewpoint of transparency, alicyclic diamines are preferred. Further, when aromatic diamines having a benzoxazole structure are used, it becomes possible to exhibit high elastic modulus, low thermal shrinkage, and low coefficient of linear expansion as well as high heat resistance. Diamines and isocyanates may be used alone or in combination of two or more.
  • aromatic diamines examples include 2,2'-dimethyl-4,4'-diaminobiphenyl, 1,4-bis[2-(4-aminophenyl)-2-propyl]benzene, 1,4-bis (4-amino-2-trifluoromethylphenoxy)benzene, 4,4'-diamino-2,2'-bis(trifluoromethyl)biphenyl, 4,4'-bis(4-aminophenoxy)biphenyl, 4, 4'-bis(3-aminophenoxy)biphenyl, bis[4-(3-aminophenoxy)phenyl]ketone, bis[4-(3-aminophenoxy)phenyl]sulfide, bis[4-(3-aminophenoxy) phenyl] sulfone, 2,2-bis[4-(3-aminophenoxy)phenyl]propane, 2,2-bis[4-(3-aminophenoxy)phenyl]-1,
  • some or all of the hydrogen atoms on the aromatic ring of the aromatic diamine may be substituted with a halogen atom, an alkyl group or alkoxyl group having 1 to 3 carbon atoms, or a cyano group, and further, Part or all of the hydrogen atoms of the alkyl group or alkoxyl group of ⁇ 3 may be substituted with a halogen atom.
  • aromatic diamines having the benzoxazole structure are not particularly limited, and examples thereof include 5-amino-2-(p-aminophenyl)benzoxazole, 6-amino-2-(p-aminophenyl)benzoxazole, Oxazole, 5-amino-2-(m-aminophenyl)benzoxazole, 6-amino-2-(m-aminophenyl)benzoxazole, 2,2'-p-phenylenebis(5-aminobenzoxazole), 2 , 2'-p-phenylenebis(6-aminobenzoxazole), 1-(5-aminobenzoxazolo)-4-(6-aminobenzoxazolo)benzene, 2,6-(4,4'-diamino) diphenyl)benzo[1,2-d:5,4-d']bisoxazole, 2,6-(4,4'-diaminodiphenyl)benzo[1,
  • aromatic diamines may be used alone or in combination.
  • alicyclic diamines examples include 1,4-diaminocyclohexane, 1,4-diamino-2-methylcyclohexane, 1,4-diamino-2-ethylcyclohexane, 1,4-diamino-2-n-propyl Cyclohexane, 1,4-diamino-2-isopropylcyclohexane, 1,4-diamino-2-n-butylcyclohexane, 1,4-diamino-2-isobutylcyclohexane, 1,4-diamino-2-sec-butylcyclohexane, Examples include 1,4-diamino-2-tert-butylcyclohexane and 4,4'-methylenebis(2,6-dimethylcyclohexylamine).
  • 1,4-diaminocyclohexane and 1,4-diamino-2-methylcyclohexane are particularly preferred, and 1,4-diaminocyclohexane is more preferred.
  • the alicyclic diamines may be used alone or in combination.
  • diisocyanates examples include diphenylmethane-2,4'-diisocyanate, 3,2'- or 3,3'- or 4,2'- or 4,3'- or 5,2'- or 5,3' - or 6,2'- or 6,3'-dimethyldiphenylmethane-2,4'-diisocyanate, 3,2'- or 3,3'- or 4,2'- or 4,3'- or 5,2 '-or 5,3'-or 6,2'-or 6,3'-diethyldiphenylmethane-2,4'-diisocyanate, 3,2'-or 3,3'-or 4,2'-or 4, 3'- or 5,2'- or 5,3'- or 6,2'- or 6,3'-dimethoxydiphenylmethane-2,4'-diisocyanate, diphenylmethane-4,4'-diisocyanate, diphenylmethane-3, 3'-diisocyanate, dipheny
  • the diisocyanates may be used alone or in combination.
  • the solvent may be any solvent as long as it can dissolve polyimide or a precursor of polyimide, and aprotic polar solvents and the like can be suitably used.
  • N,N-dilower alkylcarboxylamides such as N,N-dimethylformamide, N,N-dimethylacetamide, N,N-diethylacetamide, N,N-dimethylmethoxyacetamide, N-methyl-2-pyrrolidone , N-ethyl-2-pyrrolidone, dimethylsulfoxide, dimethylsulfone, 1,3-dimethyl-2-imidazolidinone, ⁇ -butyrolactone, diglyme, m-cresol, hexamethylphosphoramide, N-acetyl-2-pyrrolidone , hexamethylphosphoramide, ethyl cellosolve acetate, diethylene glycol dimethyl ether, sulfolane, p-chlorophenol and the
  • the thickness of the film is preferably 3 ⁇ m or more, more preferably 7 ⁇ m or more, even more preferably 14 ⁇ m or more, and even more preferably 20 ⁇ m or more.
  • the upper limit of the thickness of the film is not particularly limited, but in order to use it as a flexible electronic device, it is preferably 250 ⁇ m or less, more preferably 100 ⁇ m or less, and still more preferably 50 ⁇ m or less.
  • yellowness index When the film is a transparent polyimide film, its yellowness index (hereinafter also referred to as “yellow index” or “YI”) is preferably 10 or less, more preferably 7 or less, and still more preferably 5 or less. Yes, and even more preferably 3 or less.
  • the lower limit of the yellowness index of the transparent polyimide is not particularly limited, but in order to use it as a flexible electronic device, it is preferably 0.1 or more, more preferably 0.2 or more, and still more preferably 0.3 or more. It is.
  • the film is preferably obtained in the form of a rolled film having a width of 300 mm or more and a length of 10 m or more at the time of manufacture, and is in the form of a rolled film wound around a winding core. is more preferable.
  • When the film is wound into a roll it becomes easy to transport the film in the form of a roll.
  • lubricant particles
  • the particle size of the lubricant is preferably 20 to 500 nm, more preferably 30 to 300 nm, and even more preferably 50 to 200 nm.
  • the film manufacturing apparatus of the present invention includes: A fixing mechanism A in which fixing tools are installed at both ends in the width direction of one surface of the film before heat treatment, and the heat treated film is fixed with the fixing tools.
  • Blowing mechanism B blowing hot air to both sides of the film before heat treatment
  • Conveyance mechanism C that conveys the film before heat treatment has The blowing mechanism B is manufactured in such a manner that the speed of hot air blown to a surface where no fixture is installed is the same as or higher than the speed of hot air blown to a surface where a fixture is installed. It is a device.
  • the film and mechanisms A to C in the manufacturing apparatus have the same meaning as described in the film manufacturing method.
  • the total amount of polymer solids in the acid solution was added to be 0.15% by mass and completely dissolved, and then 9.81 parts by mass of 1,2,3,4-cyclobutanetetracarboxylic dianhydride (CBDA ), 11.34 parts by mass of 3,3',4,4'-biphenyltetracarboxylic dianhydride (BPDA), and 4.85 parts by mass of 4,4'-oxydiphthalic anhydride (ODPA). After adding the solid in portions, the mixture was stirred at room temperature for 24 hours.
  • CBDA 1,2,3,4-cyclobutanetetracarboxylic dianhydride
  • BPDA 3,3',4,4'-biphenyltetracarboxylic dianhydride
  • ODPA 4,4'-oxydiphthalic anhydride
  • PAA-A polyamic acid solution A
  • Example 1 The obtained polyamic acid solution A was applied onto the non-slip surface of polyethylene terephthalate film A4100 (manufactured by Toyobo Co., Ltd.) using a comma coater so that the final film thickness was 20 ⁇ m. This was dried at 90°C for 15 minutes. The polyamic acid film that had obtained self-supporting properties after drying was peeled off from the A4100 film used as a support to obtain a polyamic acid film (film before heat treatment). Next, a pin tenter 11 (film fixing device) was installed at the end of the lower surface of the film before heat treatment so that the pin 11a (film fixing structure) faced upward, and the end of the film before heat treatment was fixed by inserting it into the pin. .
  • a pin tenter 11 film fixing device
  • the pin sheet interval was adjusted so that the film before heat treatment would not break, and the film was conveyed at 250°C for 3 minutes from the upper air outlet to the surface where the fixture was not installed, and from the lower air outlet to the surface where the fixture was installed. , 3 minutes at 290° C., 3 minutes at 340° C., and 3 minutes at 350° C. by blowing hot air to advance the imidization reaction.
  • a hot air outlet was installed at a location 175 mm above and below the passing position of the film before heat treatment in each temperature zone, and the air velocity was 3.8 m/min from this upper outlet (in the direction of the surface where the film fixing device was not installed).
  • Hot air at a velocity of 3.6 m/sec was supplied from the lower outlet (in the direction of the film fixture installation surface). Thereafter, the film was cooled to room temperature for 2 minutes, and portions with poor flatness at both ends of the film were cut off using a slitter, and rolled up into a roll to obtain 100 m of polyimide film with a width of 500 mm.
  • Examples 2-4 The resins used and the manufacturing conditions were as shown in Table 1, and the same procedures as in Example 1 were performed to obtain polyimide films.
  • Comparative examples 1-2 The resins used and the manufacturing conditions were as shown in Table 1, and the same procedures as in Example 1 were performed to obtain polyimide films.
  • ⁇ Film appearance (edge)> The state of the film before heat treatment during transport in the furnace and the state of the end portion (fixed portion) of the film after heat treatment were visually checked and evaluated. Evaluation was performed in the following three stages. ⁇ : There is no problem with film transport, and the film can be maintained properly stretched. ⁇ : There is no problem with film transport, but the film cannot be maintained properly stretched. ⁇ : Separated or hanging due to breakage or tearing. The film comes into contact with the inner wall of the furnace and cannot be transported.
  • Total light transmittance The total light transmittance (TT) of the film was measured using HAZEMETER (NDH5000, manufactured by Nippon Denshoku Co., Ltd.). A D65 lamp was used as a light source. The arithmetic mean value of the five measured values obtained by unwinding a roll of film by 2 m, cutting out five 50 mm square films, and performing one measurement on each film was used.
  • ⁇ Film thickness> The thickness of the film was measured using a film thickness measuring device HKT-1216 (manufactured by Marl Corporation). The film was rolled up into a roll, and the film was unwound by 2.5 m, and the full width was measured at 2 cm intervals inward from any one end of the film, and the average of the measurements was taken as the thickness of the film.
  • ⁇ Tg glass transition temperature
  • the glass transition temperature was determined by cutting out a sheet of 5 mm x 20 mm from the center of the width of a 3.5 m roll of film, and using a dynamic viscoelasticity measuring device (DMA Q800 manufactured by TA Instruments). ), measurement was performed from 30° C. to 450° C. at a heating rate of 5° C./min and a frequency of 10 Hz, and the temperature at which the change in elastic modulus (mechanical tan ⁇ ) was maximum was defined as the glass transition temperature.
  • Detailed measurement conditions are as follows. Measurement mode: DMA Multi-Frequency-strain Tenshio n film/Rectangular Strain: 0.1% Preload force: 0.02N Force track: 125% Poisson's ratio: 0.440
  • the present invention can provide a film that does not cause breakage, tearing, or abnormal appearance not only at the center of the film but also at and around both ends where the film is fixed, and is suitable for, for example, flexible electronic devices. Applicable.

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Abstract

[Problem] To provide a method for producing a film such that during the production of the film, no breakage, tearing or anomalies in external appearance are caused to the film not only at the central part of the film but also at both fixed edges of the film or the vicinity thereof. [Solution] This method for producing a film comprises: a step A in which fixtures are set at both edges in the width direction of one surface of a not-yet-heat-treated film, and the not-yet-heat-treated film is fixed in place using the fixtures; a step B in which hot air is blown onto both surfaces of the not-yet-heat-treated film; and a step C in which the not-yet-heat-treated film is conveyed. In the step B, the speed of the hot air blown onto the surface where the fixtures are not set is greater than or equal to the speed of the hot air blown onto the surface where the fixtures are set.

Description

フィルムの製造方法Film manufacturing method
 本発明は、フィルムの製造方法に関する発明である。 The present invention relates to a method for producing a film.
 従来、フィルムの製造工程においては、フィルムを搬送・乾燥・熱処理などする際に、フィルムの幅方向の両端部を多数のピンやクリップで把持することにより、フィルムに対して幅方向に張力を加えた状態で搬送するテンター式搬送装置が知られている(例えば、特許文献1参照)。 Traditionally, in the film manufacturing process, tension is applied to the film in the width direction by gripping both ends of the film with multiple pins or clips when transporting, drying, or heat-treating the film. A tenter-type conveying device is known that conveys the object in a state in which the object is held (see, for example, Patent Document 1).
 テンター式搬送装置には幾つかの搬送方式がある。それらの搬送方式のうち、フィルムの両端部を、流れ方向に沿って多数のピンに突き刺すことによってフィルムを把持するピンテンター式搬送装置は、互いに平行に配置された一対の移動チェーンに把持されたピンシート上に配設された多数のピンを有する。このピンによってフィルムを把持し搬送するが、フィルムの引き裂き強度が低いと搬送中に破断することがある。 There are several transport methods for tenter-type transport devices. Among these conveyance methods, the pin tenter conveyance device grips the film by piercing both ends of the film with a large number of pins along the flow direction. It has a large number of pins arranged on the sheet. The pin grips and transports the film, but if the tear strength of the film is low, it may break during transport.
 この課題を解決するために、引き裂き強度が低いフィルムの把持部(端部)に、引き裂き強度の高いフィルムを補強フィルムとして重ね合わせることが提案されている(例えば、特許文献2参照)。 In order to solve this problem, it has been proposed to overlap a film with high tear strength as a reinforcing film on the gripping part (end) of a film with low tear strength (see, for example, Patent Document 2).
特公昭39-29211号公報Special Publication No. 39-29211 特開平11-254521号公報Japanese Patent Application Publication No. 11-254521
 しかしながら、特許文献2の方法では、引き裂き強度が低いフィルムに、引き裂き強度の高いフィルムを重ね合わせているため、原材料の無駄が多くなるという問題がある。また、このような搬送装置を用いてフィルムに熱風を当てて化学反応の進行や溶媒の揮発を行う場合、ピンによって把持されているフィルムの両端部は、ピンシートが熱風を遮るため、中央部に比べ与えられる熱風が届きにくくなる。このため、両端部に引き裂き強度の高いフィルムを重ね合わせてもフィルム両端部付近に、化学反応の未完結状態や未乾燥状態が生じ、把持部やその付近における破断や裂け、外観異常を招くことになる。このようにフィルム両端部の破断や裂けが生じると、搬送中のフィルムがピン把持部から外れ、搬送装置内にフィルムが滞留し目的のフィルムが得られなくなる。また、このような搬送装置内滞留が生じなくとも、フィルム両端部の裂けや破断は、フィルムが適切に張られた状態の維持を困難にし、その結果、フィルム全体に皺が発生するなど端部以外の品質低下の要因にもなる。さらに、フィルム両端部付近に裂けや外観異常が生じると、把持部を切断する際により中央部まで切断する必要が生じ、生産ロスの原因となる。 However, in the method of Patent Document 2, a film with high tear strength is superimposed on a film with low tear strength, so there is a problem that a large amount of raw material is wasted. In addition, when using such a conveying device to apply hot air to the film to advance a chemical reaction or volatilize the solvent, both ends of the film gripped by the pins are blocked by the pin sheets, so the central part is It is difficult for the hot air given to reach the area compared to . For this reason, even if a film with high tear strength is stacked on both ends, an unfinished state of chemical reaction or an undry state will occur near both ends of the film, resulting in breakage or tearing at the gripping part or the vicinity, and abnormal appearance. become. If both ends of the film are broken or torn in this way, the film being transported will come off the pin gripping portion, and the film will remain in the transport device, making it impossible to obtain the desired film. Furthermore, even if such accumulation in the conveying device does not occur, tearing or breaking at both ends of the film makes it difficult to maintain the proper tension of the film, and as a result, wrinkles occur throughout the film, causing damage to the edges. It can also be a cause of other quality deterioration. Furthermore, if tearing or abnormal appearance occurs near both ends of the film, it becomes necessary to cut more to the center when cutting the gripping portion, causing production loss.
 このような課題は、搬送中に化学反応の進行と溶媒揮発を同時に行う系、例えば溶媒を一定量含んだポリイミド前駆体フィルムを搬送しながら熱処理することで得られるポリイミドフィルムのような系で生じやすい。特に透明かつ高耐熱なフィルムでは、その物性を確保するために脆く裂けやすい分子構造を選択せざるを得ない場合があり、上記課題解決がボトルネックとなる。 Such problems occur in systems where chemical reactions proceed and solvent evaporates simultaneously during transport, such as systems such as polyimide films obtained by heat-treating a polyimide precursor film containing a certain amount of solvent while transporting. Cheap. In particular, in the case of transparent and highly heat-resistant films, it may be necessary to select a molecular structure that is brittle and easy to tear in order to ensure its physical properties, and solving the above problems becomes a bottleneck.
 本発明は、上述した課題に鑑みてなされたものであり、その目的は、フィルムの両端をテンター式搬送装置により固定し搬送する際に、フィルム両端部およびその付近の破断、裂けや外観異常をより効果的に抑制することが可能なフィルムの製造方法を提供することにある。 The present invention has been made in view of the above-mentioned problems, and its purpose is to prevent breakage, tearing, and appearance abnormalities at both ends of the film and the vicinity thereof when the film is transported with both ends fixed by a tenter-type transport device. It is an object of the present invention to provide a method for producing a film that can more effectively suppress the occurrence of the problem.
 本発明者らは、前記の課題を解決すべく鋭意検討した結果、本発明を完成するに至った。すなわち、本発明は以下の好適な態様を提供するものである。 The present inventors have completed the present invention as a result of intensive studies to solve the above problems. That is, the present invention provides the following preferred embodiments.
[1] フィルムの製造方法であって、
 熱処理前フィルムの一方の面の幅方向の両端部に固定具を設置し、前記固定具で前記熱処理フィルムを固定する工程A
 前記熱処理前フィルムの両面に熱風を送風する工程B
 前記熱処理前フィルムを搬送する工程C
 を有し、
 前記工程Bは、固定具を設置していない面に送風する熱風の風速が、固定具を設置している面に送風する熱風の風速と、同じかそれよりも大きいことを特徴とするフィルムの製造方法。
[2] 前記工程Bは、前記固定具を設置していない面の風速が、前記固定具を設置している面の風速の1.1倍以上である[1]に記載のフィルムの製造方法。
[3] 前記固定具がピンシートである[1]または[2]に記載のフィルムの製造方法。
[4] 前記フィルムがポリイミドフィルムである[1]~[3]のいずれかに記載のフィルムの製造方法。
[5] 前記ポリイミドフィルムが透明ポリイミドフィルムである[4]に記載のフィルムの製造方法。
[6] フィルムの製造装置であって、
 熱処理前フィルムの一方の面の幅方向の両端部に固定具を設置し、前記固定具で前記熱処理フィルムを固定する固定機構A
 前記熱処理前フィルムの両面に熱風を送風する送風機構B
 前記熱処理前フィルムを搬送する搬送機構C
 を有し、
 前記送風機構Bは、固定具を設置していない面に送風する熱風の風速が、固定具を設置している面に送風する熱風の風速と、同じかそれよりも大きいことを特徴とするフィルムの製造装置。
[7] 前記送風機構Bは、前記固定具を設置していない面の風速が、前記固定具を設置している面の風速の1.1倍以上である[6]に記載のフィルムの製造装置。
[8] 前記固定具がピンシートである[6]または[7]に記載のフィルムの製造装置。
[9] 前記フィルムがポリイミドフィルムである[6]~[8]のいずれかに記載のフィルムの製造装置。
[10] 前記ポリイミドフィルムが透明ポリイミドフィルムである[9]に記載のフィルムの製造装置。
[1] A method for producing a film, comprising:
Step A of installing fixtures at both ends in the width direction of one side of the film before heat treatment, and fixing the heat treated film with the fixtures;
Step B of blowing hot air onto both sides of the film before heat treatment
Step C of conveying the film before heat treatment
has
The process B is characterized in that the speed of the hot air blown to the surface where the fixing device is not installed is the same as or higher than the speed of the hot air blown to the surface where the fixing device is installed. Production method.
[2] The method for producing a film according to [1], wherein in the step B, the wind speed on the surface where the fixing device is not installed is 1.1 times or more the wind speed on the surface where the fixing device is installed. .
[3] The method for producing a film according to [1] or [2], wherein the fixture is a pin sheet.
[4] The method for producing a film according to any one of [1] to [3], wherein the film is a polyimide film.
[5] The method for producing a film according to [4], wherein the polyimide film is a transparent polyimide film.
[6] A film manufacturing device,
A fixing mechanism A in which fixing tools are installed at both ends in the width direction of one surface of the film before heat treatment, and the heat treated film is fixed with the fixing tools.
Blowing mechanism B blowing hot air to both sides of the film before heat treatment
Conveyance mechanism C that conveys the film before heat treatment
has
The blowing mechanism B is a film characterized in that the speed of the hot air blown to the surface where the fixing device is not installed is the same as or higher than the speed of the hot air blown to the surface where the fixing device is installed. manufacturing equipment.
[7] The production of the film according to [6], wherein the air blowing mechanism B has a wind speed on a surface where the fixing device is not installed is 1.1 times or more as a wind speed on the surface where the fixing device is installed. Device.
[8] The film manufacturing apparatus according to [6] or [7], wherein the fixture is a pin sheet.
[9] The film manufacturing apparatus according to any one of [6] to [8], wherein the film is a polyimide film.
[10] The film manufacturing apparatus according to [9], wherein the polyimide film is a transparent polyimide film.
 本発明によれば、フィルムの製造において、フィルム中央部のみならず、フィルムを固定した両端部やその付近にも破断や裂け、外観異常が生じないフィルムの製造方法を提供することができる。 According to the present invention, it is possible to provide a method for manufacturing a film that does not cause breakage, tearing, or abnormal appearance not only at the center of the film but also at and around both ends where the film is fixed.
 フィルム両端部に破断や裂けが生じると、搬送中のフィルムがフィルム固定構造(例えば、ピン)から外れ、搬送装置内にフィルムが滞留し目的のフィルムが得られなくなる。また、このような搬送装置内滞留が生じなくとも、フィルム両端部の裂けや破断は、フィルムが適切に張られた状態の維持を困難にし、その結果、フィルム全体に皺が発生するなど端部以外の品質低下の要因にもなる。さらに、フィルム両端部付近に裂けや外観異常が生じると、固定部(把持部)を切断する際により中央部まで切断する必要が生じ、生産ロスの原因となる。 If a break or tear occurs at both ends of the film, the film being transported will come off the film fixing structure (for example, a pin), and the film will remain in the transport device, making it impossible to obtain the desired film. Furthermore, even if such accumulation in the conveying device does not occur, tearing or breaking at both ends of the film makes it difficult to maintain the proper tension of the film, and as a result, wrinkles occur throughout the film, causing damage to the edges. It can also be a cause of other quality deterioration. Furthermore, if tearing or abnormal appearance occurs near both ends of the film, it becomes necessary to cut more to the center when cutting the fixing part (grip part), causing production loss.
 これに対して、本発明によれば、フィルム両端部の破断、裂けに起因したフィルム搬送不良を抑制できる。また、両端部の異常に起因した中央部の皺も抑制でき、安定した品質のフィルムを提供できる。さらに、フィルム両端部付近の破断、裂け、外観異常をも抑制できるため、切断する両端部を小さくすることができ、生産ロスを軽減できる。また、本発明の手法を用いれば、フィルム中央部に過剰な熱を与えることがないので、フィルム中央部に異常を引き起こすことなく、安定した品質のフィルムを提供できる。 On the other hand, according to the present invention, film transport defects caused by breakage and tearing of both ends of the film can be suppressed. Furthermore, wrinkles in the center caused by abnormalities at both ends can be suppressed, and a film of stable quality can be provided. Furthermore, since breakage, tearing, and abnormal appearance near both ends of the film can be suppressed, both ends to be cut can be made smaller, and production loss can be reduced. Furthermore, by using the method of the present invention, excessive heat is not applied to the center of the film, so a film of stable quality can be provided without causing abnormalities in the center of the film.
本発明の搬送中のフィルムの状態を模式的に示す説明図An explanatory diagram schematically showing the state of the film during transport of the present invention 本発明の搬送中のフィルムの他の状態を模式的に示す説明図尚、図1,2において、熱風は上下各3点から吹き出しているのではなく、吹出口の幅方向全体から均等に吹き出している。また、吹出口はフィルムの搬送方向に複数配置されている。An explanatory diagram schematically showing another state of the film during conveyance according to the present invention.In addition, in FIGS. 1 and 2, the hot air is not blown out from three points each at the top and bottom, but is blown out evenly from the entire width direction of the air outlet. ing. In addition, a plurality of air outlets are arranged in the film transport direction.
 以下、本発明の実施形態について説明する。なお、本発明の範囲はここで説明する実施の形態に限定されるものではなく、本発明の趣旨を損なわない範囲で種々の変更をすることができる。 Hereinafter, embodiments of the present invention will be described. Note that the scope of the present invention is not limited to the embodiments described here, and various changes can be made without departing from the spirit of the present invention.
 フィルムを製造する場合に、熱処理前フィルムを、加熱炉内に通過させることで有機溶剤を揮発させたり、化学反応を起こしたり、各種物性の向上をはかることがある。ここで、有機溶剤を揮発させる目的のフィルムは乾燥前のフィルムであり、化学反応を起こす目的のフィルムは前駆体フィルム(グリーンフィルム)であるが、本明細書では、これらを併せて熱処理前フィルムという。 When manufacturing a film, the film before heat treatment may be passed through a heating furnace to volatilize organic solvents, cause chemical reactions, and improve various physical properties. Here, the film for the purpose of volatilizing the organic solvent is the film before drying, and the film for the purpose of causing a chemical reaction is the precursor film (green film), but in this specification, these are collectively referred to as the film before heat treatment. That's what it means.
 このように熱処理前フィルムを加熱炉内に通過させる場合、熱処理前フィルムの一方の面の幅方向の両端部に固定具を設置し、前記固定具で前記熱処理フィルムを固定する必要がある(工程A)。固定方法は特に限定されない。搬送中に加熱処理するときは、一般的にテンター式搬送装置を用いることがある。テンター式搬送装置を用いる場合には、前記熱処理前フィルムの両端部を、ピンテンター式搬送装置の複数のピンに突き刺すことにより固定することが好ましい。熱処理前フィルムは前記両端部のみで固定することが好ましい。前記両端部のみで固定することで、熱処理前フィルムの両端部以外の箇所(例えば、中央部)の送風が遮られなくなる。上記テンター式搬送装置内で熱処理前フィルムを加熱する場合、加熱源として熱風発生機構が用いられることが多い。熱風発生機構では、熱処理前フィルムの固定具非設置面(例えば、熱処理前フィルムの上側の面)及び熱処理前フィルムの固定具設置面(例えば、熱処理前フィルムの下側の面)に熱風を吹きつけて、これにより加熱をする(工程B)。加熱処理することにより、熱処理前フィルムの有機溶剤を揮発させたり、化学反応を起こしたり、各種物性の向上をはかることができる。前記熱処理前フィルムの固定具非設置面の熱風の風速を固定具設置面の熱風の風速と、同じかそれよりも大きくすることが必要である。ここで、熱処理前フィルムに熱風を送風することを熱処理ともいう。 When the pre-heat-treated film is passed through a heating furnace in this way, it is necessary to install fixing tools at both ends in the width direction of one side of the pre-heat-treated film, and fix the heat-treated film with the fixing tools (step A). The fixing method is not particularly limited. When heat treatment is performed during transportation, a tenter-type transportation device is generally used. When using a tenter-type conveyance device, it is preferable to fix both ends of the film before heat treatment by piercing a plurality of pins of the pin tenter-type conveyance device. Preferably, the film before heat treatment is fixed only at both ends. By fixing only at both ends, air blowing at a location other than both ends (for example, the center) of the film before heat treatment is not blocked. When heating the film before heat treatment in the tenter-type conveying device, a hot air generation mechanism is often used as the heating source. The hot air generation mechanism blows hot air onto the surface of the film before heat treatment where the fixing device is not installed (e.g., the upper surface of the film before heat treatment) and the surface of the film before heat treatment where the fixer is installed (e.g., the lower surface of the film before heat treatment). and heat it (Step B). By heat treatment, it is possible to volatilize the organic solvent in the film before heat treatment, cause a chemical reaction, and improve various physical properties. It is necessary that the speed of the hot air on the surface of the film before heat treatment on which the fixture is not installed is equal to or higher than the speed of the hot air on the surface where the fixture is installed. Here, blowing hot air onto the film before heat treatment is also referred to as heat treatment.
 次いで、前記熱処理とともに熱処理前フィルムを搬送する(工程C)。 Next, along with the heat treatment, the film before heat treatment is transported (Step C).
 図1は、本発明の搬送中の熱処理前フィルムの状態を模式的に示す説明図である。熱処理前フィルムは紙面の奥側から手前側(または手前側から奥側)に搬送されている。熱処理前フィルム1の固定具設置面(下側の面)にピンシート11(フィルム固定具)を設置し、熱処理前フィルム1の両端部を、ピンシート11の上面に備えるピン11a(フィルム固定構造)に突き刺すことで固定(把持)する。そして、この状態で熱処理前フィルム1が熱処理されることになる。熱処理は、熱処理前フィルム1の固定具非設置面側(上側の面)に備えた熱風吹出口21から発生する熱風31と、その反対側の固定具設置面側(下側の面)に備えた熱風吹出口22から発生する熱風32を熱処理前フィルム1の上下両面から同時に吹きつけることで行われる。この際、熱風31はピンシート11に遮られることなく熱処理前フィルム1に吹きつけられるが、熱風32の一部は、ピンシート11に遮られることになり、熱処理前フィルム端部1bに届かない。熱風32の熱処理前フィルム中央部1aへの吹きつけは、熱風31同様、遮られることなく吹きつけられる。通常であれば、このことが原因となり、熱処理前フィルム端部1bは化学反応の未完結状態や溶媒の未乾燥状態を引き起こすこととなる。また、熱処理前フィルム端部1bへの熱風31(ピンシート11に遮られることのない熱風)の吹き付け量を増やそうとするあまり、熱風31と熱風32の合計風量を増やしてしまうと、製品となるフィルム中央部1aに過剰な熱が与えられ、過乾燥等を原因とした白濁、黄変、破断といった異常を引き起こすことになる。しかしながら、本発明によれば、熱風31と熱風32の合計風量は変えずに、熱風31の風速を熱風32の風速と同じかそれよりも大きくすることで、熱風32(ピンシート11に遮られる熱風)の割合を減らして、熱風31(ピンシート11に遮られることのない熱風)の割合を増すことになるので、フィルム端部1bにより効率的に熱風を当てることができるようになり、製品となるフィルム中央部1aに前記異常を引き起こすことなく、熱処理前フィルム端部1bにおける前記状態を回避することができる。図1では、熱処理前フィルム1の熱風吹出口21側が固定具非設置面、熱風吹出口22側が固定具設置面となる。 FIG. 1 is an explanatory diagram schematically showing the state of the film before heat treatment during transportation according to the present invention. The film before heat treatment is conveyed from the back side of the page to the front side (or from the front side to the back side). A pin sheet 11 (film fixing device) is installed on the fixing device installation surface (lower surface) of the film 1 before heat treatment, and both ends of the film 1 before heat treatment are attached to pins 11a (film fixing structure) provided on the top surface of the pin sheet 11. ) to fix (grasp) it. Then, in this state, the pre-heat-treated film 1 is heat-treated. The heat treatment is performed using hot air 31 generated from a hot air outlet 21 provided on the non-fixing device installation surface side (upper surface) of the film 1 before heat treatment, and hot air 31 generated from the hot air outlet 21 provided on the non-fixing device installation surface side (lower surface) of the film 1 before heat treatment. This is done by simultaneously blowing hot air 32 generated from a hot air outlet 22 from both upper and lower surfaces of the film 1 before heat treatment. At this time, the hot air 31 is blown onto the pre-heat-treated film 1 without being blocked by the pin sheet 11, but a part of the hot air 32 is blocked by the pin sheet 11 and does not reach the edge 1b of the pre-heat-treated film. . Like the hot air 31, the hot air 32 is blown unobstructed to the central portion 1a of the film before heat treatment. Normally, this would cause the end portion 1b of the film before heat treatment to undergo an incomplete state of chemical reaction or an undried state of the solvent. In addition, if the total amount of hot air 31 and hot air 32 is increased in an attempt to increase the amount of hot air 31 (hot air that is not blocked by pin sheet 11) blown onto the film end 1b before heat treatment, the product may become damaged. Excessive heat is applied to the central portion 1a of the film, causing abnormalities such as clouding, yellowing, and breakage due to excessive drying. However, according to the present invention, by increasing the wind speed of hot air 31 to be the same as or higher than that of hot air 32 without changing the total volume of hot air 31 and hot air 32, hot air 32 (which is blocked by pin sheet 11) This reduces the proportion of hot air (hot air) and increases the proportion of hot air 31 (hot air that is not blocked by the pin sheet 11), making it possible to more efficiently apply hot air to the film edge 1b, thereby improving the quality of the product. The above-mentioned condition at the end portion 1b of the film before heat treatment can be avoided without causing the above-mentioned abnormality in the central portion 1a of the film. In FIG. 1, the hot air outlet 21 side of the film 1 before heat treatment is the non-fixing device installation surface, and the hot air outlet 22 side is the fixing device installation surface.
 本発明は、図2にあるように熱処理前フィルムの上側の面にピンテンター11を設置し、熱処理前フィルム1両端部を、ピンシート11の下側の面に備えるピン11aに突き刺すことで固定してもよい。この場合、熱処理前フィルム1の固定具非設置面側(下側の面)の熱風31の風速を、熱処理前フィルム1の固定具設置面側(上側の面)の熱風32の風速と同じか、それよりも大きくする。図2では、熱処理前フィルム1の熱風吹出口22側が固定具設置面、熱風吹出口21側が固定具非設置面となる。 In the present invention, as shown in FIG. 2, a pin tenter 11 is installed on the upper surface of the film before heat treatment, and both ends of the film 1 before heat treatment are fixed by piercing pins 11a provided on the lower surface of the pin sheet 11. You can. In this case, the wind speed of the hot air 31 on the side of the film 1 before heat treatment where the fixing device is not installed (lower side) is the same as the wind speed of the hot air 32 on the side of the film 1 before heat treatment where the fixing device is installed (the upper side). , make it larger than that. In FIG. 2, the hot air outlet 22 side of the film 1 before heat treatment is the fixture installation surface, and the hot air outlet 21 side is the fixture non-installation surface.
 前記ピンテンター式搬送装置は、一般に互いに平行に配置された一対の移動チェーンに固定(把持)されたピンシート上に配設された多数のピンを有する。このピンシートに配設されたピンは、ピンシートの上側の面であっても、下側の面であってもよい。ピンの配置は特に限定されず、従来公知のもの等を用いることができる。 The pin tenter type conveying device generally has a large number of pins arranged on a pin sheet fixed (grasped) by a pair of moving chains arranged parallel to each other. The pins arranged on this pin sheet may be on the upper surface or the lower surface of the pin sheet. The arrangement of the pins is not particularly limited, and conventionally known pins can be used.
 熱処理前フィルムの固定具非設置面および固定具設置面に送風する(吹きつける)熱風の温度は、溶媒揮発や化学反応の促進のため、80℃以上500℃以下であることが好ましい。熱処理前フィルムに含まれる溶媒を除去しやすく、また、熱処理前フィルムがポリイミドの前駆体(ポリアミド酸)である場合は、イミド化(熱イミド化)しやすくなることから、120℃以上がより好ましく、150℃以上が更に好ましく、200℃以上が特に好ましい。また、フィルムの熱によるダメージを抑えられることから、より好ましくは450℃以下であり、さらに好ましくは400℃以下であり、特に好ましくは380℃以下である。前記範囲内であると、搬送中にフィルムの破断や裂けを抑え、フィルムの品質が良好となる。固定具非設置面および固定具設置面の熱風温度は、それぞれ同じであってもよく、異なっていてもよい、装置の簡素化から同じ温度であることが好ましい。フィルム搬送中の熱風の温度の変化は特に限定されず、複数の加熱炉を接続して熱風の温度を段階的に変化するような設計であってもよく、熱風の温度が搬送方向に向かって徐々に上がる、もしくは下がるような設計であってもよい。複数の加熱炉内で熱処理する場合、加熱炉は2個以上10個以下であることが好ましく、より好ましくは3個以上8個以下であり、さらに好ましくは4個以上6個以下である。複数の加熱炉内で熱処理することで、熱処理前フィルムを段階的に乾燥させたり、熱イミド化させることができ、それによりフィルムの品質が向上する。 It is preferable that the temperature of the hot air blown (blown) on the non-fixing device installation surface and the fixing device installation surface of the film before heat treatment is 80° C. or higher and 500° C. or lower in order to promote solvent volatilization and chemical reactions. The temperature is more preferably 120°C or higher because it is easy to remove the solvent contained in the film before heat treatment, and when the film before heat treatment is a polyimide precursor (polyamic acid), it is easy to imidize (thermal imidization). , more preferably 150°C or higher, particularly preferably 200°C or higher. Further, since damage to the film due to heat can be suppressed, the temperature is more preferably 450°C or lower, still more preferably 400°C or lower, and particularly preferably 380°C or lower. Within the above range, breakage and tearing of the film during transportation is suppressed, and the quality of the film is improved. The hot air temperatures on the fixture-free surface and the fixture-installed surface may be the same or different, but are preferably the same temperature from the viewpoint of simplifying the apparatus. Changes in the temperature of the hot air during film transport are not particularly limited, and the design may be such that multiple heating furnaces are connected to change the temperature of the hot air in stages. It may be designed to gradually rise or fall. When heat treatment is performed in a plurality of heating furnaces, the number of heating furnaces is preferably 2 or more and 10 or less, more preferably 3 or more and 8 or less, and even more preferably 4 or more and 6 or less. By performing heat treatment in multiple heating furnaces, the film before heat treatment can be dried in stages or thermally imidized, thereby improving the quality of the film.
 熱処理前フィルムの固定具非設置面に送風する熱風の風速は、0.5m/秒以上15m/秒以下であることが好ましい。熱風が熱処理前フィルムに十分届き、熱処理前フィルムに含まれる溶媒を除去しやすく、また、熱処理前フィルムがポリイミドの前駆体(ポリアミド酸)である場合は、イミド化(熱イミド化)しやすくなることから、より好ましくは1m/秒以上であり、さらに好ましくは1.5m/秒以上であり、よりさらに好ましくは2m/秒以上であり、特に好ましくは3m/秒以上である。また、熱処理前フィルムのばたつきによる破断や裂け、ピン外れ等を抑えられることから、13m/秒以下であることが好ましく、より好ましくは12m/秒以下であり、さらに好ましくは10m/秒以下である。 It is preferable that the speed of the hot air blown to the surface of the film before heat treatment on which the fixing device is not installed is 0.5 m/sec or more and 15 m/sec or less. The hot air sufficiently reaches the film before heat treatment, making it easier to remove the solvent contained in the film before heat treatment, and if the film before heat treatment is a polyimide precursor (polyamic acid), it becomes easier to imidize (thermal imidization). Therefore, it is more preferably 1 m/sec or more, still more preferably 1.5 m/sec or more, even more preferably 2 m/sec or more, and particularly preferably 3 m/sec or more. In addition, the speed is preferably 13 m/sec or less, more preferably 12 m/sec or less, and even more preferably 10 m/sec or less, since it can suppress breakage, tearing, pin detachment, etc. due to flapping of the film before heat treatment. .
 熱処理前フィルムの固定具設置面に送風する熱風の風速は、0.4m/秒以上14m/秒以下であることが好ましい。熱処理前フィルムに含まれる溶媒を除去しやすく、また、熱処理前フィルムがポリイミドの前駆体(ポリアミド酸)である場合は、イミド化(熱イミド化)しやすくなることから、より好ましくは0.9m/秒以上であり、さらに好ましくは1.4m/秒以上であり、よりさらに好ましくは1.9m/秒以上である。また、熱処理前フィルムのばたつきによる破断や裂け、ピン外れ等を抑えられることから、12m/秒以下であることが好ましく、より好ましくは11m/秒以下であり、さらに好ましくは9m/秒以下である。 It is preferable that the speed of the hot air blown onto the fixing device installation surface of the film before heat treatment is 0.4 m/sec or more and 14 m/sec or less. More preferably 0.9 m, since it is easy to remove the solvent contained in the film before heat treatment, and when the film before heat treatment is a polyimide precursor (polyamic acid), it is easy to imidize (thermal imidization). /sec or more, more preferably 1.4 m/sec or more, even more preferably 1.9 m/sec or more. In addition, the speed is preferably 12 m/sec or less, more preferably 11 m/sec or less, and even more preferably 9 m/sec or less, since it can suppress breakage, tearing, pin detachment, etc. due to flapping of the film before heat treatment. .
 前記熱処理前フィルムの固定具非設置面に送風する熱風の風速は、固定具設置面に送風する熱風の風速と、同じかそれよりも大きいことが必要である。固定具非設置面と固定具設置面との風速の比率(固定具非設置面/固定具設置面)は、1.0超であることが好ましい。固定具(ピンシート11)に遮られる熱風の比率を抑え、熱処理前フィルム両端部に熱風が十分届き、熱処理前フィルムの両端部の乾燥や化学反応が完結しやすくなることから、好ましくは1.05以上であり、より好ましくは1.1以上である。また、固定具設置面側の空間の温度低下、および前記温度低下に伴うフィルム自体の温度低下を抑え、熱処理前フィルム全体の乾燥や化学反応が完結しやすくなることから、好ましくは10以下であり、より好ましくは5以下であり、さらに好ましくは3以下である。 The speed of the hot air blown to the surface of the pre-heat-treated film on which the fixing device is not installed needs to be the same as or higher than the speed of the hot air blown to the surface where the fixing device is installed. The ratio of wind speeds between the fixture non-installation surface and the fixture installation surface (fixture non-installation surface/fixture installation surface) is preferably greater than 1.0. Preferably, 1. 05 or more, more preferably 1.1 or more. In addition, it is preferably 10 or less because it suppresses the temperature drop in the space on the side where the fixture is installed and the temperature drop in the film itself due to the temperature drop, making it easier to dry the entire film before heat treatment and complete the chemical reaction. , more preferably 5 or less, still more preferably 3 or less.
 前記熱処理前フィルムの固定具非設置面に送風する熱風の風速が、固定具設置面に送風する熱風の風速よりも小さいと、フィルム固定具によって遮られる熱風の比率が増大し、熱処理前フィルム端部に当たる熱風が減少することになる。このため、熱処理前フィルム端部は熱処理前フィルム中央部に比べて、乾燥や化学反応の完結までにより多くの時間が必要となる。このフィルム端部のみ乾燥や化学反応が未完の状態であるとき、フィルム端部は十分な強度を得られておらず、フィルム固定構造(ピン11a)を起点とした裂けや伸び等の外観異常を引き起こすことがある。この異常が顕著に生じると、破断したフィルムが炉内出口等にひっかかることで滞留し、フィルム搬送自体が困難になることがある。また、このようなフィルム端部を起点とした外観異常は、端部に留まらずフィルム中央部付近にまで及ぶ可能性があり、品質低下や生産ロスの原因となる。 If the speed of the hot air blown to the surface of the pre-heat-treated film on which the fixing device is not installed is smaller than the speed of the hot air blown to the surface where the fixing device is installed, the proportion of the hot air blocked by the film fixing device increases, and the edge of the film before heat treatment increases. This will reduce the amount of hot air hitting the area. Therefore, the edges of the film before heat treatment require more time to dry and complete the chemical reaction than the center of the film before heat treatment. When only the edges of the film are dry or the chemical reaction is not completed, the edges of the film do not have sufficient strength, and appearance abnormalities such as tearing and elongation may occur starting from the film fixing structure (pin 11a). It may cause If this abnormality occurs significantly, the broken film may get caught in the outlet of the furnace and remain there, making it difficult to transport the film itself. In addition, such abnormal appearance starting from the edges of the film may not be limited to the edges but may extend to the vicinity of the center of the film, causing quality deterioration and production loss.
 熱処理した乾燥後のフィルムに含まれる残留溶媒は、500ppm以下であることが好ましく、より好ましくは200ppm以下であり、さらに好ましくは100ppm以下である。残留溶媒量は少ないほどよいが、工業的には1ppm以上であってもよく、10ppm以上であっても差し支えない。 The residual solvent contained in the heat-treated and dried film is preferably 500 ppm or less, more preferably 200 ppm or less, and still more preferably 100 ppm or less. The smaller the amount of residual solvent, the better; however, from an industrial perspective, it may be 1 ppm or more, and even 10 ppm or more.
 本発明のフィルムは、幅が300mm以上、長さが10m以上の長尺フィルムとして巻き取られる方式により製造されるものであることが好ましい。また、熱処理前フィルムの一方の面の幅方向の両端部を固定する方法は特に限定されず、ピンテンター式搬送装置のピンに突き刺して把持してもよいし、クリップテンター式搬送装置のクリップで挟むことにより把持してもよい。 The film of the present invention is preferably manufactured by a method in which it is wound up as a long film having a width of 300 mm or more and a length of 10 m or more. Furthermore, the method for fixing both widthwise ends of one side of the film before heat treatment is not particularly limited, and may be held by sticking it into a pin of a pin tenter-type conveyance device, or by holding it with a clip of a clip tenter-type conveyance device. It may also be gripped.
 前記両端部の幅(各端部の幅)は、従来公知のテンター式搬送装置にて固定することが可能な幅であれば、特に限定されない。具体的には、下限としては、好ましくは5mm以上であり、より好ましくは10mm以上である。または、両端部の幅の合計が熱処理前フィルム全幅の0.1%以上であることが好ましく、より好ましくは0.5%以上であり、さらに好ましくは1%以上である。
 また、前記両端部の幅(各端部の幅)の上限としては、好ましくは100mm以下であり、より好ましくは50mm以下である。または、両端部の幅の合計がフィルム全幅の50%以下であることが好ましく、より好ましくは30%以下であり、さらに好ましくは10%以下である。
The width of both ends (width of each end) is not particularly limited as long as it can be fixed using a conventionally known tenter-type conveyance device. Specifically, the lower limit is preferably 5 mm or more, more preferably 10 mm or more. Alternatively, the total width of both ends is preferably 0.1% or more of the total width of the film before heat treatment, more preferably 0.5% or more, and still more preferably 1% or more.
Further, the upper limit of the width of both ends (width of each end) is preferably 100 mm or less, more preferably 50 mm or less. Alternatively, the total width of both ends is preferably at most 50% of the total width of the film, more preferably at most 30%, even more preferably at most 10%.
 熱処理前フィルムの幅方向における中央部は、熱処理前フィルム全幅を100%としたとき、一方の端から30~70%となる位置であることが好ましく、より好ましくは40~60%となる位置であり、さらに好ましくは45~55%となる位置である。 The central part in the width direction of the film before heat treatment is preferably a position 30 to 70% from one end, more preferably 40 to 60% when the full width of the film before heat treatment is 100%. The position is more preferably 45 to 55%.
 熱処理前フィルムの搬送速度は、熱処理条件(熱風の温度や風速等)により適宜設定できる。適正な搬送速度は熱処理炉の炉長に依存するため厳密に定めることは難しいが、遅いと生産性の低下を招くおそれがある。好ましくは0.05m/分以上であり、より好ましくは0.1m/分以上である。 The transport speed of the film before heat treatment can be appropriately set depending on the heat treatment conditions (hot air temperature, wind speed, etc.). Although it is difficult to determine an appropriate conveying speed strictly because it depends on the length of the heat treatment furnace, if it is slow, there is a risk that productivity will decrease. Preferably it is 0.05 m/min or more, more preferably 0.1 m/min or more.
<フィルム>
 本発明のフィルム(熱処理後フィルム)としては、ポリイミド、ポリアミドイミド、ポリエーテルイミド、フッ素化ポリイミドといったポリイミド系樹脂(例えば、芳香族ポリイミド樹脂、脂環族ポリイミド樹脂);ポリエチレン、ポリプロピレンといったポリオレフィン系樹脂;ポリエチレンテレフタレート、ポリブチレンテレフタレート、ポリエチレン-2,6-ナフタレートといった共重合ポリエステル(例えば、全芳香族ポリエステル、半芳香族ポリエステル);ポリメチルメタクリレートに代表される共重合(メタ)アクリレート;ポリカーボネート;ポリアミド;ポリスルフォン;ポリエーテルスルフォン;ポリエーテルケトン;酢酸セルロース;硝酸セルロース;芳香族ポリアミド;ポリ塩化ビニル;ポリフェノール;ポリアリレート;ポリフェニレンスルフィド;ポリフェニレンオキシド;ポリスチレン等のフィルムを例示できる。
<Film>
The film of the present invention (film after heat treatment) includes polyimide resins such as polyimide, polyamideimide, polyetherimide, and fluorinated polyimide (e.g., aromatic polyimide resin, alicyclic polyimide resin); polyolefin resins such as polyethylene and polypropylene. ; Copolymerized polyesters such as polyethylene terephthalate, polybutylene terephthalate, and polyethylene-2,6-naphthalate (e.g., fully aromatic polyesters, semi-aromatic polyesters); Copolymerized (meth)acrylates represented by polymethyl methacrylate; Polycarbonates; Polyamides ; polysulfone; polyethersulfone; polyetherketone; cellulose acetate; cellulose nitrate; aromatic polyamide; polyvinyl chloride; polyphenol; polyarylate; polyphenylene sulfide; polyphenylene oxide; polystyrene.
 前記フィルムは、250℃以上の熱処理を伴うプロセスに好適に用いられることが前提であるため、例示された高分子フィルムの中から実際に適用できる物は限られる。前記フィルムのなかでも好ましくは、所謂スーパーエンジニアリングプラスチックを用いたフィルムであり、より具体的には、ポリイミド系樹脂、ポリアミド系樹脂、ポリアミドイミド系樹脂、アゾール系樹脂が挙げられる。特に好ましい具体例として、芳香族ポリイミドフィルム、芳香族アミドフィルム、芳香族アミドイミドフィルム、芳香族ベンゾオキサゾールフィルム、芳香族ベンゾチアゾールフィルム、芳香族ベンゾイミダゾールフィルム等が挙げられる。 Since the above-mentioned film is premised on being suitably used in a process involving heat treatment at 250° C. or higher, there are a limited number of polymer films that can actually be used among the exemplified polymer films. Among the above films, preferred are films using so-called super engineering plastics, more specifically polyimide resins, polyamide resins, polyamideimide resins, and azole resins. Particularly preferred specific examples include aromatic polyimide film, aromatic amide film, aromatic amide-imide film, aromatic benzoxazole film, aromatic benzothiazole film, aromatic benzimidazole film, and the like.
 本発明の熱処理前フィルムは、前記フィルムに有機溶媒を含有するフィルム(乾燥前フィルム)、化学反応前のフィルム(前駆体フィルム)、または、有機溶媒を含有する前駆体フィルム(乾燥前前駆体フィルム)等が挙げられる。
 熱処理前フィルムの有機溶媒含有量としては、熱処理前フィルム両端を固定(把持)して搬送できることから、好ましくは50質量%以下であり、より好ましくは45質量%以下であり、さらに好ましくは40質量%以下である。また、製造効率やコストの観点から、好ましくは10質量%以上であり、より好ましくは15質量%以上であり、さらに好ましくは20質量%以上である。
The film before heat treatment of the present invention is a film containing an organic solvent in the film (pre-drying film), a film before chemical reaction (precursor film), or a precursor film containing an organic solvent (dried precursor film). ) etc.
The organic solvent content of the film before heat treatment is preferably 50% by mass or less, more preferably 45% by mass or less, and even more preferably 40% by mass, since both ends of the film before heat treatment can be fixed (held) and transported. % or less. Further, from the viewpoint of manufacturing efficiency and cost, the content is preferably 10% by mass or more, more preferably 15% by mass or more, and still more preferably 20% by mass or more.
 以下に前記フィルムの一例であるポリイミド系樹脂フィルム(ポリイミドフィルムと称する場合もある)についての詳細を説明する。一般にポリイミド系樹脂フィルムは、溶媒中でジアミン類とテトラカルボン酸類とを反応させて得られるポリアミド酸(ポリイミド前駆体)溶液を、ポリイミドフィルム作製用支持体に塗布、乾燥してグリーンフィルム(以下では「ポリアミド酸フィルム」ともいう)とし、さらにポリイミドフィルム作製用支持体上で、あるいは該支持体から剥がした状態でグリーンフィルムを高温熱処理して脱水閉環反応を行わせることによって得られる。このポリアミド酸フィルムが、ポリイミドの前駆体フィルムである。 The details of a polyimide resin film (sometimes referred to as a polyimide film), which is an example of the film, will be described below. Generally, polyimide resin films are produced by applying a polyamic acid (polyimide precursor) solution obtained by reacting diamines and tetracarboxylic acids in a solvent to a support for polyimide film production, and drying it to form a green film (hereinafter referred to as green film). (also referred to as a "polyamic acid film"), and is obtained by further heat-treating the green film at a high temperature on a support for producing a polyimide film or in a state peeled from the support to perform a dehydration ring-closing reaction. This polyamic acid film is a polyimide precursor film.
 ポリアミド酸(ポリイミド前駆体であり、以下ポリアミック酸ともいう。)溶液の塗布は、例えば、スピンコート、ドクターブレード、アプリケーター、コンマコーター、スクリーン印刷法、スリットコート、リバースコート、ディップコート、カーテンコート、スリットダイコート等従来公知の溶液の塗布手段を適宜用いることができる。 Application of polyamic acid (polyimide precursor, hereinafter also referred to as polyamic acid) solution can be performed using, for example, spin coating, doctor blade, applicator, comma coater, screen printing method, slit coating, reverse coating, dip coating, curtain coating, Conventionally known solution coating means such as slit die coating can be used as appropriate.
 ポリアミック酸を構成するジアミン類としては、特に制限はなく、ポリイミド合成に通常用いられる芳香族ジアミン類、脂肪族ジアミン類、脂環式ジアミン類等を用いることができる。耐熱性の観点からは、芳香族ジアミン類が好ましい。ジアミン類は、単独で用いてもよいし二種以上を併用してもよい。 The diamines constituting the polyamic acid are not particularly limited, and aromatic diamines, aliphatic diamines, alicyclic diamines, etc. commonly used in polyimide synthesis can be used. From the viewpoint of heat resistance, aromatic diamines are preferred. Diamines may be used alone or in combination of two or more.
 ジアミン類としては特に限定はなく、例えばオキシジアニリン(ビス(4-アミノフェニル)エーテル)、パラフェニレンジアミン(1,4-フェニレンジアミン)等が挙げられる。 The diamines are not particularly limited, and include, for example, oxydianiline (bis(4-aminophenyl) ether), paraphenylenediamine (1,4-phenylenediamine), and the like.
 ポリアミック酸を構成するテトラカルボン酸類としては、ポリイミド合成に通常用いられる芳香族テトラカルボン酸類(その酸無水物を含む)、脂肪族テトラカルボン酸類(その酸無水物を含む)、脂環族テトラカルボン酸類(その酸無水物を含む)を用いることができる。これらが酸無水物である場合、分子内に無水物構造は1個であってもよいし2個であってもよいが、好ましくは2個の無水物構造を有するもの(二無水物)がよい。テトラカルボン酸類は単独で用いてもよいし、二種以上を併用してもよい。 Tetracarboxylic acids constituting polyamic acids include aromatic tetracarboxylic acids (including their acid anhydrides), aliphatic tetracarboxylic acids (including their acid anhydrides), and alicyclic tetracarboxylic acids that are commonly used in polyimide synthesis. Acids (including their acid anhydrides) can be used. When these are acid anhydrides, the number of anhydride structures in the molecule may be one or two, but those having two anhydride structures (dianhydride) are preferable. good. Tetracarboxylic acids may be used alone or in combination of two or more.
 テトラカルボン酸としては、特に限定はなく、例えばピロリメット酸二無水物、3,3’,4,4’-ビフェニルテトラカルボン酸二無水物等が挙げられる。 The tetracarboxylic acid is not particularly limited and includes, for example, pyrolimet dianhydride, 3,3',4,4'-biphenyltetracarboxylic dianhydride, and the like.
 前記ポリイミドフィルムは、透明ポリイミドフィルムであっても良い。 The polyimide film may be a transparent polyimide film.
 前記フィルムの一例である無色透明ポリイミドについて説明する。以下煩雑さを避けるために、単に透明ポリイミドとも記す。透明ポリイミドの透明性としては、全光線透過率が75%以上のものであることが好ましい。より好ましくは80%以上であり、さらに好ましくは83%以上であり、より一層好ましくは84%以上であり、特に好ましくは85%以上である。前記透明ポリイミドの全光線透過率の上限は特に制限されないが、フレキシブル電子デバイスとして用いるためには98%以下であることが好ましく、より好ましくは97%以下である。本発明における無色透明ポリイミドとは、全光線透過率75%以上のポリイミドが好ましい。 A colorless and transparent polyimide, which is an example of the film, will be explained. Hereinafter, to avoid complexity, it will also be simply referred to as transparent polyimide. Regarding the transparency of the transparent polyimide, it is preferable that the total light transmittance is 75% or more. It is more preferably 80% or more, still more preferably 83% or more, even more preferably 84% or more, particularly preferably 85% or more. The upper limit of the total light transmittance of the transparent polyimide is not particularly limited, but for use as a flexible electronic device, it is preferably 98% or less, more preferably 97% or less. The colorless transparent polyimide in the present invention is preferably a polyimide having a total light transmittance of 75% or more.
 無色透明性の高いポリイミドを得るための芳香族テトラカルボン酸類としては、4,4’-(2,2-ヘキサフルオロイソプロピリデン)ジフタル酸、4,4’-オキシジフタル酸、ビス(1,3-ジオキソ-1,3-ジヒドロ-2-ベンゾフラン-5-カルボン酸)1,4-フェニレン、ビス(1,3-ジオキソ-1,3-ジヒドロ-2-ベンゾフラン-5-イル)ベンゼン-1,4-ジカルボキシレート、4,4’-[4,4’-(3-オキソ-1,3-ジヒドロ-2-ベンゾフラン-1,1-ジイル)ビス(ベンゼン-1,4-ジイルオキシ)]ジベンゼン-1、2-ジカルボン酸、3,3’,4,4’-ベンゾフェノンテトラカルボン酸、4,4’-[(3-オキソ-1,3-ジヒドロ-2-ベンゾフラン-1,1-ジイル)ビス(トルエン-2,5-ジイルオキシ)]ジベンゼン-1、2-ジカルボン酸、4,4’-[(3-オキソ-1,3-ジヒドロ-2-ベンゾフラン-1,1-ジイル)ビス(1,4-キシレン-2,5-ジイルオキシ)]ジベンゼン-1、2-ジカルボン酸、4,4’-[4,4’-(3-オキソ-1,3-ジヒドロ-2-ベンゾフラン-1,1-ジイル)ビス(4-イソプロピル―トルエン-2,5-ジイルオキシ)]ジベンゼン-1、2-ジカルボン酸、4,4’-[4,4’-(3-オキソ-1,3-ジヒドロ-2-ベンゾフラン-1,1-ジイル)ビス(ナフタレン-1,4-ジイルオキシ)]ジベンゼン-1、2-ジカルボン酸、4,4’-[4,4’-(3H-2,1-ベンズオキサチオール-1,1-ジオキシド-3,3-ジイル)ビス(ベンゼン-1,4-ジイルオキシ)]ジベンゼン-1、2-ジカルボン酸、4,4’-ベンゾフェノンテトラカルボン酸、4,4’-[(3H-2,1-ベンズオキサチオール-1,1-ジオキシド-3,3-ジイル)ビス(トルエン-2,5-ジイルオキシ)]ジベンゼン-1、2-ジカルボン酸、4,4’-[(3H-2,1-ベンズオキサチオール-1,1-ジオキシド-3,3-ジイル)ビス(1,4-キシレン-2,5-ジイルオキシ)]ジベンゼン-1、2-ジカルボン酸、4,4’-[4,4’-(3H-2,1-ベンズオキサチオール-1,1-ジオキシド-3,3-ジイル)ビス(4-イソプロピル―トルエン-2,5-ジイルオキシ)]ジベンゼン-1、2-ジカルボン酸、4,4’-[4,4’-(3H-2,1-ベンズオキサチオール-1,1-ジオキシド-3,3-ジイル)ビス(ナフタレン-1,4-ジイルオキシ)]ジベンゼン-1、2-ジカルボン酸、3,3’,4,4’-ベンゾフェノンテトラカルボン酸、3,3’,4,4’-ベンゾフェノンテトラカルボン酸、3,3’,4,4’-ジフェニルスルホンテトラカルボン酸、3,3’,4,4’-ビフェニルテトラカルボン酸、2,3,3’,4’-ビフェニルテトラカルボン酸、ピロメリット酸、4,4’-[スピロ(キサンテン-9,9’-フルオレン)-2,6-ジイルビス(オキシカルボニル)]ジフタル酸、4,4’-[スピロ(キサンテン-9,9’-フルオレン)-3,6-ジイルビス(オキシカルボニル)]ジフタル酸、などのテトラカルボン酸及びこれらの酸無水物が挙げられる。これらの中でも、2個の酸無水物構造を有する二無水物が好適であり、特に、4,4’-(2,2-ヘキサフルオロイソプロピリデン)ジフタル酸二無水物、4,4’-オキシジフタル酸二無水物が好ましい。なお、芳香族テトラカルボン酸類は単独で用いてもよいし、二種以上を併用してもよい。芳香族テトラカルボン酸類の共重合量は、耐熱性を重視する場合には、例えば、全テトラカルボン酸類の50質量%以上が好ましく、より好ましくは60質量%以上であり、さらに好ましくは70質量%以上であり、なおさらに好ましくは80質量%以上であり、特に好ましくは90質量%以上であり、100質量%であっても差し支えない。 Aromatic tetracarboxylic acids for obtaining colorless and highly transparent polyimide include 4,4'-(2,2-hexafluoroisopropylidene)diphthalic acid, 4,4'-oxydiphthalic acid, and bis(1,3- dioxo-1,3-dihydro-2-benzofuran-5-carboxylic acid) 1,4-phenylene, bis(1,3-dioxo-1,3-dihydro-2-benzofuran-5-yl)benzene-1,4 -dicarboxylate, 4,4'-[4,4'-(3-oxo-1,3-dihydro-2-benzofuran-1,1-diyl)bis(benzene-1,4-diyloxy)]dibenzene- 1,2-dicarboxylic acid, 3,3',4,4'-benzophenonetetracarboxylic acid, 4,4'-[(3-oxo-1,3-dihydro-2-benzofuran-1,1-diyl)bis (Toluene-2,5-diyloxy)]dibenzene-1,2-dicarboxylic acid, 4,4'-[(3-oxo-1,3-dihydro-2-benzofuran-1,1-diyl)bis(1, 4-xylene-2,5-diyloxy)]dibenzene-1,2-dicarboxylic acid, 4,4'-[4,4'-(3-oxo-1,3-dihydro-2-benzofuran-1,1- diyl)bis(4-isopropyl-toluene-2,5-diyloxy)]dibenzene-1,2-dicarboxylic acid, 4,4'-[4,4'-(3-oxo-1,3-dihydro-2- benzofuran-1,1-diyl)bis(naphthalene-1,4-diyloxy)]dibenzene-1,2-dicarboxylic acid, 4,4'-[4,4'-(3H-2,1-benzoxathiol-) 1,1-dioxide-3,3-diyl)bis(benzene-1,4-diyloxy)]dibenzene-1,2-dicarboxylic acid, 4,4'-benzophenonetetracarboxylic acid, 4,4'-[(3H -2,1-benzoxathiol-1,1-dioxide-3,3-diyl)bis(toluene-2,5-diyloxy)]dibenzene-1,2-dicarboxylic acid, 4,4'-[(3H- 2,1-Benzoxathiol-1,1-dioxide-3,3-diyl)bis(1,4-xylene-2,5-diyloxy)]dibenzene-1,2-dicarboxylic acid, 4,4'-[ 4,4'-(3H-2,1-benzoxathiol-1,1-dioxide-3,3-diyl)bis(4-isopropyl-toluene-2,5-diyloxy)]dibenzene-1,2-dicarvone Acid, 4,4'-[4,4'-(3H-2,1-benzoxathiol-1,1-dioxide-3,3-diyl)bis(naphthalene-1,4-diyloxy)]dibenzene-1 , 2-dicarboxylic acid, 3,3',4,4'-benzophenone tetracarboxylic acid, 3,3',4,4'-benzophenone tetracarboxylic acid, 3,3',4,4'-diphenylsulfone tetracarboxylic acid acid, 3,3',4,4'-biphenyltetracarboxylic acid, 2,3,3',4'-biphenyltetracarboxylic acid, pyromellitic acid, 4,4'-[spiro(xanthene-9,9') -fluorene)-2,6-diylbis(oxycarbonyl)]diphthalic acid, 4,4'-[spiro(xanthene-9,9'-fluorene)-3,6-diylbis(oxycarbonyl)]diphthalic acid, etc. Examples include tetracarboxylic acids and their acid anhydrides. Among these, dianhydrides having two acid anhydride structures are preferred, particularly 4,4'-(2,2-hexafluoroisopropylidene)diphthalic dianhydride, 4,4'-oxydiphthalic dianhydride, Acid dianhydrides are preferred. Incidentally, the aromatic tetracarboxylic acids may be used alone or in combination of two or more kinds. When heat resistance is important, the amount of copolymerized aromatic tetracarboxylic acids is preferably 50% by mass or more of the total tetracarboxylic acids, more preferably 60% by mass or more, and still more preferably 70% by mass. The content is more preferably 80% by mass or more, particularly preferably 90% by mass or more, and may be 100% by mass.
 脂環式テトラカルボン酸類としては、1,2,3,4-シクロブタンテトラカルボン酸、1,2,3,4-シクロペンタンテトラカルボン酸、1,2,3,4-シクロヘキサンテトラカルボン酸、1,2,4,5-シクロヘキサンテトラカルボン酸、3,3’,4,4’-ビシクロヘキシルテトラカルボン酸、ビシクロ[2,2、1]ヘプタン-2,3,5,6-テトラカルボン酸、ビシクロ[2,2,2]オクタン-2,3,5,6-テトラカルボン酸、ビシクロ[2,2,2]オクト-7-エン-2,3,5,6-テトラカルボン酸、テトラヒドロアントラセン-2,3,6,7-テトラカルボン酸、テトラデカヒドロ-1,4:5,8:9,10-トリメタノアントラセン-2,3,6,7-テトラカルボン酸、デカヒドロナフタレン-2,3,6,7-テトラカルボン酸、デカヒドロ-1,4:5,8-ジメタノナフタレン-2,3,6,7-テトラカルボン酸、デカヒドロ-1,4-エタノ-5,8-メタノナフタレン-2,3,6,7-テトラカルボン酸、ノルボルナン-2-スピロ-α-シクロペンタノン-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸(別名「ノルボルナン-2-スピロ-2’-シクロペンタノン-5’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸」)、メチルノルボルナン-2-スピロ-α-シクロペンタノン-α’-スピロ-2’’-(メチルノルボルナン)-5,5’’,6,6’’-テトラカルボン酸、ノルボルナン-2-スピロ-α-シクロヘキサノン-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸(別名「ノルボルナン-2-スピロ-2’-シクロヘキサノン-6’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸」)、メチルノルボルナン-2-スピロ-α-シクロヘキサノン-α’-スピロ-2’’-(メチルノルボルナン)-5,5’’,6,6’’-テトラカルボン酸、ノルボルナン-2-スピロ-α-シクロプロパノン-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸、ノルボルナン-2-スピロ-α-シクロブタノン-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸、ノルボルナン-2-スピロ-α-シクロヘプタノン-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸、ノルボルナン-2-スピロ-α-シクロオクタノン-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸、ノルボルナン-2-スピロ-α-シクロノナノン-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸、ノルボルナン-2-スピロ-α-シクロデカノン-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸、ノルボルナン-2-スピロ-α-シクロウンデカノン-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸、ノルボルナン-2-スピロ-α-シクロドデカノン-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸、ノルボルナン-2-スピロ-α-シクロトリデカノン-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸、ノルボルナン-2-スピロ-α-シクロテトラデカノン-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸、ノルボルナン-2-スピロ-α-シクロペンタデカノン-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸、ノルボルナン-2-スピロ-α-(メチルシクロペンタノン)-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸、ノルボルナン-2-スピロ-α-(メチルシクロヘキサノン)-α’-スピロ-2’’-ノルボルナン-5,5’’,6,6’’-テトラカルボン酸、などのテトラカルボン酸及びこれらの酸無水物が挙げられる。これらの中でも、2個の酸無水物構造を有する二無水物が好適であり、特に、1,2,3,4-シクロブタンテトラカルボン酸二無水物、1,2,3,4-シクロヘキサンテトラカルボン酸二無水物、1,2,4,5-シクロヘキサンテトラカルボン酸二無水物が好ましく、1,2,3,4-シクロブタンテトラカルボン酸二無水物、1,2,4,5-シクロヘキサンテトラカルボン酸二無水物がより好ましく、1,2,3,4-シクロブタンテトラカルボン酸二無水物がさらに好ましい。なお、これらは単独で用いてもよいし、二種以上を併用してもよい。脂環式テトラカルボン酸類の共重合量は、透明性を重視する場合には、例えば、全テトラカルボン酸類の50質量%以上が好ましく、より好ましくは60質量%以上であり、さらに好ましくは70質量%以上であり、なおさらに好ましくは80質量%以上であり、特に好ましくは90質量%以上であり、100質量%であっても差し支えない。 Examples of alicyclic tetracarboxylic acids include 1,2,3,4-cyclobutanetetracarboxylic acid, 1,2,3,4-cyclopentanetetracarboxylic acid, 1,2,3,4-cyclohexanetetracarboxylic acid, 1 , 2,4,5-cyclohexanetetracarboxylic acid, 3,3',4,4'-bicyclohexyltetracarboxylic acid, bicyclo[2,2,1]heptane-2,3,5,6-tetracarboxylic acid, Bicyclo[2,2,2]octane-2,3,5,6-tetracarboxylic acid, bicyclo[2,2,2]oct-7-ene-2,3,5,6-tetracarboxylic acid, tetrahydroanthracene -2,3,6,7-tetracarboxylic acid, tetradecahydro-1,4:5,8:9,10-trimethanoanthracene-2,3,6,7-tetracarboxylic acid, decahydronaphthalene-2 , 3,6,7-tetracarboxylic acid, decahydro-1,4:5,8-dimethanonaphthalene-2,3,6,7-tetracarboxylic acid, decahydro-1,4-ethano-5,8-methano Naphthalene-2,3,6,7-tetracarboxylic acid, norbornane-2-spiro-α-cyclopentanone-α'-spiro-2''-norbornane-5,5'',6,6''-tetra Carboxylic acid (also known as "norbornane-2-spiro-2'-cyclopentanone-5'-spiro-2''-norbornane-5,5'',6,6''-tetracarboxylic acid"), methylnorbornane- 2-spiro-α-cyclopentanone-α'-spiro-2''-(methylnorbornane)-5,5'',6,6''-tetracarboxylic acid, norbornane-2-spiro-α-cyclohexanone- α'-spiro-2''-norbornane-5,5'',6,6''-tetracarboxylic acid (also known as "norbornane-2-spiro-2'-cyclohexanone-6'-spiro-2''-norbornane -5,5'',6,6''-tetracarboxylic acid''), methylnorbornane-2-spiro-α-cyclohexanone-α'-spiro-2''-(methylnorbornane)-5,5'', 6,6''-tetracarboxylic acid, norbornane-2-spiro-α-cyclopropanone-α'-spiro-2''-norbornane-5,5'',6,6''-tetracarboxylic acid, norbornane -2-spiro-α-cyclobutanone-α'-spiro-2''-norbornane-5,5'',6,6''-tetracarboxylic acid, norbornane-2-spiro-α-cycloheptanone-α' -spiro-2''-norbornane-5,5'',6,6''-tetracarboxylic acid, norbornane-2-spiro-α-cyclooctanone-α'-spiro-2''-norbornane-5, 5'',6,6''-tetracarboxylic acid, norbornane-2-spiro-α-cyclononanone-α'-spiro-2''-norbornane-5,5'',6,6''-tetracarboxylic acid , norbornane-2-spiro-α-cyclodecanone-α'-spiro-2''-norbornane-5,5'',6,6''-tetracarboxylic acid, norbornane-2-spiro-α-cycloundecanone- α'-spiro-2''-norbornane-5,5'',6,6''-tetracarboxylic acid, norbornane-2-spiro-α-cyclododecanone-α'-spiro-2''-norbornane- 5,5'',6,6''-tetracarboxylic acid, norbornane-2-spiro-α-cyclotridecanone-α'-spiro-2''-norbornane-5,5'',6,6'' -tetracarboxylic acid, norbornane-2-spiro-α-cyclotetradecanone-α'-spiro-2''-norbornane-5,5'',6,6''-tetracarboxylic acid, norbornane-2-spiro -α-cyclopentadecanone-α'-spiro-2''-norbornane-5,5'',6,6''-tetracarboxylic acid, norbornane-2-spiro-α-(methylcyclopentanone)- α'-spiro-2''-norbornane-5,5'',6,6''-tetracarboxylic acid, norbornane-2-spiro-α-(methylcyclohexanone)-α'-spiro-2''-norbornane Examples include tetracarboxylic acids such as -5,5'',6,6''-tetracarboxylic acid, and acid anhydrides thereof. Among these, dianhydrides having two acid anhydride structures are preferred, particularly 1,2,3,4-cyclobutanetetracarboxylic dianhydride and 1,2,3,4-cyclohexanetetracarboxylic dianhydride. Acid dianhydride, 1,2,4,5-cyclohexanetetracarboxylic dianhydride is preferred, and 1,2,3,4-cyclobutanetetracarboxylic dianhydride, 1,2,4,5-cyclohexanetetracarboxylic dianhydride Acid dianhydride is more preferred, and 1,2,3,4-cyclobutanetetracarboxylic dianhydride is even more preferred. Note that these may be used alone or in combination of two or more. When emphasis is placed on transparency, the amount of copolymerized alicyclic tetracarboxylic acids is, for example, preferably 50% by mass or more of the total tetracarboxylic acids, more preferably 60% by mass or more, and still more preferably 70% by mass. % or more, still more preferably 80% by mass or more, particularly preferably 90% by mass or more, and may even be 100% by mass.
 トリカルボン酸類としては、トリメリット酸、1,2,5-ナフタレントリカルボン酸、ジフェニルエーテル-3,3’,4’-トリカルボン酸、ジフェニルスルホン-3,3’,4’-トリカルボン酸などの芳香族トリカルボン酸、或いはヘキサヒドロトリメリット酸などの上記芳香族トリカルボン酸の水素添加物、エチレングリコールビストリメリテート、プロピレングリコールビストリメリテート、1,4-ブタンジオールビストリメリテート、ポリエチレングリコールビストリメリテートなどのアルキレングリコールビストリメリテート、及びこれらの一無水物、エステル化物が挙げられる。これらの中でも、1個の酸無水物構造を有する一無水物が好適であり、特に、トリメリット酸無水物、ヘキサヒドロトリメリット酸無水物が好ましい。尚、これらは単独で使用してもよいし複数を組み合わせて使用してもよい。 Examples of tricarboxylic acids include aromatic tricarboxylic acids such as trimellitic acid, 1,2,5-naphthalene tricarboxylic acid, diphenyl ether-3,3',4'-tricarboxylic acid, and diphenylsulfone-3,3',4'-tricarboxylic acid. acids, or hydrogenated products of the above aromatic tricarboxylic acids such as hexahydrotrimellitic acid, alkylenes such as ethylene glycol bis trimellitate, propylene glycol bis trimellitate, 1,4-butanediol bis trimellitate, and polyethylene glycol bis trimellitate. Examples include glycol bistrimelitate, and monoanhydrides and esterified products thereof. Among these, monoanhydrides having one acid anhydride structure are preferred, and trimellitic anhydride and hexahydrotrimellitic anhydride are particularly preferred. Incidentally, these may be used alone or in combination.
 ジカルボン酸類としては、テレフタル酸、イソフタル酸、オルソフタル酸、ナフタレンジカルボン酸、4、4’-オキシジベンゼンカルボン酸などの芳香族ジカルボン酸、或いは1,6-シクロヘキサンジカルボン酸などの上記芳香族ジカルボン酸の水素添加物、シュウ酸、コハク酸、グルタル酸、アジピン酸、ヘプタン二酸、オクタン二酸、アゼライン酸、セバシン酸、ウンデカ二酸、ドデカン二酸、2-メチルコハク酸、及びこれらの酸塩化物或いはエステル化物などが挙げられる。これらの中で芳香族ジカルボン酸及びその水素添加物が好適であり、特に、テレフタル酸、1,6-シクロヘキサンジカルボン酸、4、4’-オキシジベンゼンカルボン酸が好ましい。尚、ジカルボン酸類は単独で使用してもよいし複数を組み合わせて使用してもよい。 Examples of dicarboxylic acids include aromatic dicarboxylic acids such as terephthalic acid, isophthalic acid, orthophthalic acid, naphthalene dicarboxylic acid, 4,4'-oxydibenzenecarboxylic acid, or the above-mentioned aromatic dicarboxylic acids such as 1,6-cyclohexanedicarboxylic acid. Hydrogenates of oxalic acid, succinic acid, glutaric acid, adipic acid, heptanedioic acid, octanedioic acid, azelaic acid, sebacic acid, undecanedioic acid, dodecanedioic acid, 2-methylsuccinic acid, and acid chlorides thereof Alternatively, examples include esterified products. Among these, aromatic dicarboxylic acids and hydrogenated products thereof are preferred, with terephthalic acid, 1,6-cyclohexanedicarboxylic acid, and 4,4'-oxydibenzenecarboxylic acid being particularly preferred. Note that dicarboxylic acids may be used alone or in combination.
 無色透明性の高いポリイミドを得るためのジアミン類或いはイソシアネート類としては、特に制限はなく、ポリイミド合成、ポリアミドイミド合成、ポリアミド合成に通常用いられる芳香族ジアミン類、脂肪族ジアミン類、脂環式ジアミン類、芳香族ジイソシアネート類、脂肪族ジイソシアネート類、脂環式ジイソシアネート類等を用いることができる。耐熱性の観点からは、芳香族ジアミン類が好ましく、透明性の観点からは脂環式ジアミン類が好ましい。また、ベンゾオキサゾール構造を有する芳香族ジアミン類を用いると、高い耐熱性とともに、高弾性率、低熱収縮性、低線膨張係数を発現させることが可能になる。ジアミン類及びイソシアネート類は、単独で用いてもよいし二種以上を併用してもよい。 Diamines or isocyanates for obtaining colorless and highly transparent polyimides are not particularly limited, and include aromatic diamines, aliphatic diamines, and alicyclic diamines commonly used in polyimide synthesis, polyamide-imide synthesis, and polyamide synthesis. diisocyanates, aromatic diisocyanates, aliphatic diisocyanates, alicyclic diisocyanates, etc. can be used. From the viewpoint of heat resistance, aromatic diamines are preferred, and from the viewpoint of transparency, alicyclic diamines are preferred. Further, when aromatic diamines having a benzoxazole structure are used, it becomes possible to exhibit high elastic modulus, low thermal shrinkage, and low coefficient of linear expansion as well as high heat resistance. Diamines and isocyanates may be used alone or in combination of two or more.
 芳香族ジアミン類としては、例えば、2,2’-ジメチル-4,4’-ジアミノビフェニル、1,4-ビス[2-(4-アミノフェニル)-2-プロピル]ベンゼン、1,4-ビス(4-アミノ-2-トリフルオロメチルフェノキシ)ベンゼン、4,4’-ジアミノ-2,2’-ビス(トリフルオロメチル)ビフェニル、4,4’-ビス(4-アミノフェノキシ)ビフェニル、4,4’-ビス(3-アミノフェノキシ)ビフェニル、ビス[4-(3-アミノフェノキシ)フェニル]ケトン、ビス[4-(3-アミノフェノキシ)フェニル]スルフィド、ビス[4-(3-アミノフェノキシ)フェニル]スルホン、2,2-ビス[4-(3-アミノフェノキシ)フェニル]プロパン、2,2-ビス[4-(3-アミノフェノキシ)フェニル]-1,1,1,3,3,3-ヘキサフルオロプロパン、m-フェニレンジアミン、o-フェニレンジアミン、p-フェニレンジアミン、m-アミノベンジルアミン、p-アミノベンジルアミン、4-アミノ-N-(4-アミノフェニル)ベンズアミド、3,3’-ジアミノジフェニルエーテル、3,4’-ジアミノジフェニルエーテル、4,4’-ジアミノジフェニルエーテル、2,2’-トリフルオロメチル-4,4’-ジアミノジフェニルエーテル、3,3’-ジアミノジフェニルスルフィド、3,4’-ジアミノジフェニルスルフィド、4,4’-ジアミノジフェニルスルフィド、3,3’-ジアミノジフェニルスルホキシド、3,4’-ジアミノジフェニルスルホキシド、4,4’-ジアミノジフェニルスルホキシド、3,3’-ジアミノジフェニルスルホン、3,4’-ジアミノジフェニルスルホン、4,4’-ジアミノジフェニルスルホン、3,3’-ジアミノベンゾフェノン、3,4’-ジアミノベンゾフェノン、4,4’-ジアミノベンゾフェノン、3,3’-ジアミノジフェニルメタン、3,4’-ジアミノジフェニルメタン、4,4’-ジアミノジフェニルメタン、ビス[4-(4-アミノフェノキシ)フェニル]メタン、1,1-ビス[4-(4-アミノフェノキシ)フェニル]エタン、1,2-ビス[4-(4-アミノフェノキシ)フェニル]エタン、1,1-ビス[4-(4-アミノフェノキシ)フェニル]プロパン、1,2-ビス[4-(4-アミノフェノキシ)フェニル]プロパン、1,3-ビス[4-(4-アミノフェノキシ)フェニル]プロパン、2,2-ビス[4-(4-アミノフェノキシ)フェニル]プロパン、1,1-ビス[4-(4-アミノフェノキシ)フェニル]ブタン、1,3-ビス[4-(4-アミノフェノキシ)フェニル]ブタン、1,4-ビス[4-(4-アミノフェノキシ)フェニル]ブタン、2,2-ビス[4-(4-アミノフェノキシ)フェニル]ブタン、2,3-ビス[4-(4-アミノフェノキシ)フェニル]ブタン、2-[4-(4-アミノフェノキシ)フェニル]-2-[4-(4-アミノフェノキシ)-3-メチルフェニル]プロパン、2,2-ビス[4-(4-アミノフェノキシ)-3-メチルフェニル]プロパン、2-[4-(4-アミノフェノキシ)フェニル]-2-[4-(4-アミノフェノキシ)-3,5-ジメチルフェニル]プロパン、2,2-ビス[4-(4-アミノフェノキシ)-3,5-ジメチルフェニル]プロパン、2,2-ビス[4-(4-アミノフェノキシ)フェニル]-1,1,1,3,3,3-ヘキサフルオロプロパン、1,4-ビス(3-アミノフェノキシ)ベンゼン、1,3-ビス(3-アミノフェノキシ)ベンゼン、1,4-ビス(4-アミノフェノキシ)ベンゼン、4,4’-ビス(4-アミノフェノキシ)ビフェニル、ビス[4-(4-アミノフェノキシ)フェニル]ケトン、ビス[4-(4-アミノフェノキシ)フェニル]スルフィド、ビス[4-(4-アミノフェノキシ)フェニル]スルホキシド、ビス[4-(4-アミノフェノキシ)フェニル]スルホン、ビス[4-(3-アミノフェノキシ)フェニル]エーテル、ビス[4-(4-アミノフェノキシ)フェニル]エーテル、1,3-ビス[4-(4-アミノフェノキシ)ベンゾイル]ベンゼン、1,3-ビス[4-(3-アミノフェノキシ)ベンゾイル]ベンゼン、1,4-ビス[4-(3-アミノフェノキシ)ベンゾイル]ベンゼン、4,4’-ビス[(3-アミノフェノキシ)ベンゾイル]ベンゼン、1,1-ビス[4-(3-アミノフェノキシ)フェニル]プロパン、1,3-ビス[4-(3-アミノフェノキシ)フェニル]プロパン、3,4’-ジアミノジフェニルスルフィド、2,2-ビス[3-(3-アミノフェノキシ)フェニル]-1,1,1,3,3,3-ヘキサフルオロプロパン、ビス[4-(3-アミノフェノキシ)フェニル]メタン、1,1-ビス[4-(3-アミノフェノキシ)フェニル]エタン、1,2-ビス[4-(3-アミノフェノキシ)フェニル]エタン、ビス[4-(3-アミノフェノキシ)フェニル]スルホキシド、4,4’-ビス[3-(4-アミノフェノキシ)ベンゾイル]ジフェニルエーテル、4,4’-ビス[3-(3-アミノフェノキシ)ベンゾイル]ジフェニルエーテル、4,4’-ビス[4-(4-アミノ-α,α-ジメチルベンジル)フェノキシ]ベンゾフェノン、4,4’-ビス[4-(4-アミノ-α,α-ジメチルベンジル)フェノキシ]ジフェニルスルホン、ビス[4-{4-(4-アミノフェノキシ)フェノキシ}フェニル]スルホン、1,4-ビス[4-(4-アミノフェノキシ)フェノキシ-α,α-ジメチルベンジル]ベンゼン、1,3-ビス[4-(4-アミノフェノキシ)フェノキシ-α,α-ジメチルベンジル]ベンゼン、1,3-ビス[4-(4-アミノ-6-トリフルオロメチルフェノキシ)-α,α-ジメチルベンジル]ベンゼン、1,3-ビス[4-(4-アミノ-6-フルオロフェノキシ)-α,α-ジメチルベンジル]ベンゼン、1,3-ビス[4-(4-アミノ-6-メチルフェノキシ)-α,α-ジメチルベンジル]ベンゼン、1,3-ビス[4-(4-アミノ-6-シアノフェノキシ)-α,α-ジメチルベンジル]ベンゼン、3,3’-ジアミノ-4,4’-ジフェノキシベンゾフェノン、4,4’-ジアミノ-5,5’-ジフェノキシベンゾフェノン、3,4’-ジアミノ-4,5’-ジフェノキシベンゾフェノン、3,3’-ジアミノ-4-フェノキシベンゾフェノン、4,4’-ジアミノ-5-フェノキシベンゾフェノン、3,4’-ジアミノ-4-フェノキシベンゾフェノン、3,4’-ジアミノ-5’-フェノキシベンゾフェノン、3,3’-ジアミノ-4,4’-ジビフェノキシベンゾフェノン、4,4’-ジアミノ-5,5’-ジビフェノキシベンゾフェノン、3,4’-ジアミノ-4,5’-ジビフェノキシベンゾフェノン、3,3’-ジアミノ-4-ビフェノキシベンゾフェノン、4,4’-ジアミノ-5-ビフェノキシベンゾフェノン、3,4’-ジアミノ-4-ビフェノキシベンゾフェノン、3,4’-ジアミノ-5’-ビフェノキシベンゾフェノン、1,3-ビス(3-アミノ-4-フェノキシベンゾイル)ベンゼン、1,4-ビス(3-アミノ-4-フェノキシベンゾイル)ベンゼン、1,3-ビス(4-アミノ-5-フェノキシベンゾイル)ベンゼン、1,4-ビス(4-アミノ-5-フェノキシベンゾイル)ベンゼン、1,3-ビス(3-アミノ-4-ビフェノキシベンゾイル)ベンゼン、1,4-ビス(3-アミノ-4-ビフェノキシベンゾイル)ベンゼン、1,3-ビス(4-アミノ-5-ビフェノキシベンゾイル)ベンゼン、1,4-ビス(4-アミノ-5-ビフェノキシベンゾイル)ベンゼン、2,6-ビス[4-(4-アミノ-α,α-ジメチルベンジル)フェノキシ]ベンゾニトリル、4,4’-[9H-フルオレン-9,9-ジイル]ビスアニリン(別名「9,9-ビス(4-アミノフェニル)フルオレン」)、スピロ(キサンテン-9,9’-フルオレン)-2,6-ジイルビス(オキシカルボニル)]ビスアニリン、4,4’-[スピロ(キサンテン-9,9’-フルオレン)-2,6-ジイルビス(オキシカルボニル)]ビスアニリン、4,4’-[スピロ(キサンテン-9,9’-フルオレン)-3,6-ジイルビス(オキシカルボニル)]ビスアニリン等が挙げられる。また、上記芳香族ジアミンの芳香環上の水素原子の一部もしくは全てが、ハロゲン原子、炭素数1~3のアルキル基もしくはアルコキシル基、またはシアノ基で置換されても良く、さらに前記炭素数1~3のアルキル基もしくはアルコキシル基の水素原子の一部もしくは全部がハロゲン原子で置換されても良い。また、前記ベンゾオキサゾール構造を有する芳香族ジアミン類としては、特に限定はなく、例えば、5-アミノ-2-(p-アミノフェニル)ベンゾオキサゾール、6-アミノ-2-(p-アミノフェニル)ベンゾオキサゾール、5-アミノ-2-(m-アミノフェニル)ベンゾオキサゾール、6-アミノ-2-(m-アミノフェニル)ベンゾオキサゾール、2,2’-p-フェニレンビス(5-アミノベンゾオキサゾール)、2,2’-p-フェニレンビス(6-アミノベンゾオキサゾール)、1-(5-アミノベンゾオキサゾロ)-4-(6-アミノベンゾオキサゾロ)ベンゼン、2,6-(4,4’-ジアミノジフェニル)ベンゾ[1,2-d:5,4-d’]ビスオキサゾール、2,6-(4,4’-ジアミノジフェニル)ベンゾ[1,2-d:4,5-d’]ビスオキサゾール、2,6-(3,4’-ジアミノジフェニル)ベンゾ[1,2-d:5,4-d’]ビスオキサゾール、2,6-(3,4’-ジアミノジフェニル)ベンゾ[1,2-d:4,5-d’]ビスオキサゾール、2,6-(3,3’-ジアミノジフェニル)ベンゾ[1,2-d:5,4-d’]ビスオキサゾール、2,6-(3,3’-ジアミノジフェニル)ベンゾ[1,2-d:4,5-d’]ビスオキサゾール等が挙げられる。これらの中で、特に、4,4’-ジアミノ-2,2’-ビス(トリフルオロメチル)ビフェニル、4-アミノ-N-(4-アミノフェニル)ベンズアミド、4,4’-ジアミノジフェニルスルホン、3,3’-ジアミノベンゾフェノンが好ましい。尚、芳香族ジアミン類は単独で使用してもよいし複数を組み合わせて使用してもよい。 Examples of aromatic diamines include 2,2'-dimethyl-4,4'-diaminobiphenyl, 1,4-bis[2-(4-aminophenyl)-2-propyl]benzene, 1,4-bis (4-amino-2-trifluoromethylphenoxy)benzene, 4,4'-diamino-2,2'-bis(trifluoromethyl)biphenyl, 4,4'-bis(4-aminophenoxy)biphenyl, 4, 4'-bis(3-aminophenoxy)biphenyl, bis[4-(3-aminophenoxy)phenyl]ketone, bis[4-(3-aminophenoxy)phenyl]sulfide, bis[4-(3-aminophenoxy) phenyl] sulfone, 2,2-bis[4-(3-aminophenoxy)phenyl]propane, 2,2-bis[4-(3-aminophenoxy)phenyl]-1,1,1,3,3,3 -hexafluoropropane, m-phenylenediamine, o-phenylenediamine, p-phenylenediamine, m-aminobenzylamine, p-aminobenzylamine, 4-amino-N-(4-aminophenyl)benzamide, 3,3' -diaminodiphenyl ether, 3,4'-diaminodiphenyl ether, 4,4'-diaminodiphenyl ether, 2,2'-trifluoromethyl-4,4'-diaminodiphenyl ether, 3,3'-diaminodiphenyl sulfide, 3,4' -diaminodiphenylsulfide, 4,4'-diaminodiphenylsulfide, 3,3'-diaminodiphenylsulfoxide, 3,4'-diaminodiphenylsulfoxide, 4,4'-diaminodiphenylsulfoxide, 3,3'-diaminodiphenylsulfone, 3,4'-diaminodiphenylsulfone, 4,4'-diaminodiphenylsulfone, 3,3'-diaminobenzophenone, 3,4'-diaminobenzophenone, 4,4'-diaminobenzophenone, 3,3'-diaminodiphenylmethane, 3,4'-diaminodiphenylmethane, 4,4'-diaminodiphenylmethane, bis[4-(4-aminophenoxy)phenyl]methane, 1,1-bis[4-(4-aminophenoxy)phenyl]ethane, 1, 2-bis[4-(4-aminophenoxy)phenyl]ethane, 1,1-bis[4-(4-aminophenoxy)phenyl]propane, 1,2-bis[4-(4-aminophenoxy)phenyl] Propane, 1,3-bis[4-(4-aminophenoxy)phenyl]propane, 2,2-bis[4-(4-aminophenoxy)phenyl]propane, 1,1-bis[4-(4-amino) phenoxy)phenyl]butane, 1,3-bis[4-(4-aminophenoxy)phenyl]butane, 1,4-bis[4-(4-aminophenoxy)phenyl]butane, 2,2-bis[4- (4-aminophenoxy)phenyl]butane, 2,3-bis[4-(4-aminophenoxy)phenyl]butane, 2-[4-(4-aminophenoxy)phenyl]-2-[4-(4- aminophenoxy)-3-methylphenyl]propane, 2,2-bis[4-(4-aminophenoxy)-3-methylphenyl]propane, 2-[4-(4-aminophenoxy)phenyl]-2-[ 4-(4-aminophenoxy)-3,5-dimethylphenyl]propane, 2,2-bis[4-(4-aminophenoxy)-3,5-dimethylphenyl]propane, 2,2-bis[4- (4-aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoropropane, 1,4-bis(3-aminophenoxy)benzene, 1,3-bis(3-aminophenoxy)benzene , 1,4-bis(4-aminophenoxy)benzene, 4,4'-bis(4-aminophenoxy)biphenyl, bis[4-(4-aminophenoxy)phenyl]ketone, bis[4-(4-amino) phenoxy)phenyl] sulfide, bis[4-(4-aminophenoxy)phenyl]sulfoxide, bis[4-(4-aminophenoxy)phenyl]sulfone, bis[4-(3-aminophenoxy)phenyl]ether, bis[ 4-(4-aminophenoxy)phenyl]ether, 1,3-bis[4-(4-aminophenoxy)benzoyl]benzene, 1,3-bis[4-(3-aminophenoxy)benzoyl]benzene, 1, 4-bis[4-(3-aminophenoxy)benzoyl]benzene, 4,4'-bis[(3-aminophenoxy)benzoyl]benzene, 1,1-bis[4-(3-aminophenoxy)phenyl]propane , 1,3-bis[4-(3-aminophenoxy)phenyl]propane, 3,4'-diaminodiphenyl sulfide, 2,2-bis[3-(3-aminophenoxy)phenyl]-1,1,1 , 3,3,3-hexafluoropropane, bis[4-(3-aminophenoxy)phenyl]methane, 1,1-bis[4-(3-aminophenoxy)phenyl]ethane, 1,2-bis[4 -(3-aminophenoxy)phenyl]ethane, bis[4-(3-aminophenoxy)phenyl]sulfoxide, 4,4'-bis[3-(4-aminophenoxy)benzoyl]diphenyl ether, 4,4'-bis [3-(3-aminophenoxy)benzoyl]diphenyl ether, 4,4'-bis[4-(4-amino-α,α-dimethylbenzyl)phenoxy]benzophenone, 4,4'-bis[4-(4- Amino-α,α-dimethylbenzyl)phenoxy]diphenylsulfone, bis[4-{4-(4-aminophenoxy)phenoxy}phenyl]sulfone, 1,4-bis[4-(4-aminophenoxy)phenoxy-α , α-dimethylbenzyl]benzene, 1,3-bis[4-(4-aminophenoxy)phenoxy-α,α-dimethylbenzyl]benzene, 1,3-bis[4-(4-amino-6-trifluoro) methylphenoxy)-α,α-dimethylbenzyl]benzene, 1,3-bis[4-(4-amino-6-fluorophenoxy)-α,α-dimethylbenzyl]benzene, 1,3-bis[4-( 4-Amino-6-methylphenoxy)-α,α-dimethylbenzyl]benzene, 1,3-bis[4-(4-amino-6-cyanophenoxy)-α,α-dimethylbenzyl]benzene, 3,3 '-Diamino-4,4'-diphenoxybenzophenone, 4,4'-diamino-5,5'-diphenoxybenzophenone, 3,4'-diamino-4,5'-diphenoxybenzophenone, 3,3'- Diamino-4-phenoxybenzophenone, 4,4'-diamino-5-phenoxybenzophenone, 3,4'-diamino-4-phenoxybenzophenone, 3,4'-diamino-5'-phenoxybenzophenone, 3,3'-diamino -4,4'-Dibiphenoxybenzophenone, 4,4'-diamino-5,5'-dibiphenoxybenzophenone, 3,4'-diamino-4,5'-dibiphenoxybenzophenone, 3,3'-diamino-4 -Biphenoxybenzophenone, 4,4'-diamino-5-biphenoxybenzophenone, 3,4'-diamino-4-biphenoxybenzophenone, 3,4'-diamino-5'-biphenoxybenzophenone, 1,3-bis (3-amino-4-phenoxybenzoyl)benzene, 1,4-bis(3-amino-4-phenoxybenzoyl)benzene, 1,3-bis(4-amino-5-phenoxybenzoyl)benzene, 1,4- Bis(4-amino-5-phenoxybenzoyl)benzene, 1,3-bis(3-amino-4-biphenoxybenzoyl)benzene, 1,4-bis(3-amino-4-biphenoxybenzoyl)benzene, 1 , 3-bis(4-amino-5-biphenoxybenzoyl)benzene, 1,4-bis(4-amino-5-biphenoxybenzoyl)benzene, 2,6-bis[4-(4-amino-α, α-dimethylbenzyl)phenoxy]benzonitrile, 4,4'-[9H-fluorene-9,9-diyl]bisaniline (also known as "9,9-bis(4-aminophenyl)fluorene"), spiro(xanthene-9 ,9'-fluorene)-2,6-diylbis(oxycarbonyl)]bisaniline, 4,4'-[spiro(xanthene-9,9'-fluorene)-2,6-diylbis(oxycarbonyl)]bisaniline, 4 , 4'-[spiro(xanthene-9,9'-fluorene)-3,6-diylbis(oxycarbonyl)]bisaniline, and the like. Further, some or all of the hydrogen atoms on the aromatic ring of the aromatic diamine may be substituted with a halogen atom, an alkyl group or alkoxyl group having 1 to 3 carbon atoms, or a cyano group, and further, Part or all of the hydrogen atoms of the alkyl group or alkoxyl group of ~3 may be substituted with a halogen atom. Further, the aromatic diamines having the benzoxazole structure are not particularly limited, and examples thereof include 5-amino-2-(p-aminophenyl)benzoxazole, 6-amino-2-(p-aminophenyl)benzoxazole, Oxazole, 5-amino-2-(m-aminophenyl)benzoxazole, 6-amino-2-(m-aminophenyl)benzoxazole, 2,2'-p-phenylenebis(5-aminobenzoxazole), 2 , 2'-p-phenylenebis(6-aminobenzoxazole), 1-(5-aminobenzoxazolo)-4-(6-aminobenzoxazolo)benzene, 2,6-(4,4'-diamino) diphenyl)benzo[1,2-d:5,4-d']bisoxazole, 2,6-(4,4'-diaminodiphenyl)benzo[1,2-d:4,5-d']bisoxazole , 2,6-(3,4'-diaminodiphenyl)benzo[1,2-d:5,4-d']bisoxazole, 2,6-(3,4'-diaminodiphenyl)benzo[1,2 -d:4,5-d']bisoxazole, 2,6-(3,3'-diaminodiphenyl)benzo[1,2-d:5,4-d']bisoxazole, 2,6-(3 , 3'-diaminodiphenyl)benzo[1,2-d:4,5-d']bisoxazole, and the like. Among these, in particular, 4,4'-diamino-2,2'-bis(trifluoromethyl)biphenyl, 4-amino-N-(4-aminophenyl)benzamide, 4,4'-diaminodiphenylsulfone, 3,3'-diaminobenzophenone is preferred. Incidentally, the aromatic diamines may be used alone or in combination.
 脂環式ジアミン類としては、例えば、1,4-ジアミノシクロヘキサン、1,4-ジアミノ-2-メチルシクロヘキサン、1,4-ジアミノ-2-エチルシクロヘキサン、1,4-ジアミノ-2-n-プロピルシクロヘキサン、1,4-ジアミノ-2-イソプロピルシクロヘキサン、1,4-ジアミノ-2-n-ブチルシクロヘキサン、1,4-ジアミノ-2-イソブチルシクロヘキサン、1,4-ジアミノ-2-sec-ブチルシクロヘキサン、1,4-ジアミノ-2-tert-ブチルシクロヘキサン、4,4’-メチレンビス(2,6-ジメチルシクロヘキシルアミン)等が挙げられる。これらの中で、特に、1,4-ジアミノシクロヘキサン、1,4-ジアミノ-2-メチルシクロヘキサンが好ましく、1,4-ジアミノシクロヘキサンがより好ましい。尚、脂環式ジアミン類は単独で使用してもよいし複数を組み合わせて使用してもよい。 Examples of alicyclic diamines include 1,4-diaminocyclohexane, 1,4-diamino-2-methylcyclohexane, 1,4-diamino-2-ethylcyclohexane, 1,4-diamino-2-n-propyl Cyclohexane, 1,4-diamino-2-isopropylcyclohexane, 1,4-diamino-2-n-butylcyclohexane, 1,4-diamino-2-isobutylcyclohexane, 1,4-diamino-2-sec-butylcyclohexane, Examples include 1,4-diamino-2-tert-butylcyclohexane and 4,4'-methylenebis(2,6-dimethylcyclohexylamine). Among these, 1,4-diaminocyclohexane and 1,4-diamino-2-methylcyclohexane are particularly preferred, and 1,4-diaminocyclohexane is more preferred. Incidentally, the alicyclic diamines may be used alone or in combination.
 ジイソシアネート類としては、例えば、ジフェニルメタン-2,4’-ジイソシアネート、3,2’-または3,3’-または4,2’-または4,3’-または5,2’-または5,3’-または6,2’-または6,3’-ジメチルジフェニルメタン-2,4’-ジイソシアネート、3,2’-または3,3’-または4,2’-または4,3’-または5,2’-または5,3’-または6,2’-または6,3’-ジエチルジフェニルメタン-2,4’-ジイソシアネート、3,2’-または3,3’-または4,2’-または4,3’-または5,2’-または5,3’-または6,2’-または6,3’-ジメトキシジフェニルメタン-2,4’-ジイソシアネート、ジフェニルメタン-4,4’-ジイソシアネート、ジフェニルメタン-3,3’-ジイソシアネート、ジフェニルメタン-3,4’-ジイソシアネート、ジフェニルエーテル-4,4’ -ジイソシアネート、ベンゾフェノン-4,4’-ジイソシアネート、ジフェニルスルホン-4,4’-ジイソシアネート、トリレン-2,4-ジイソシアネート、トリレン-2,6-ジイソシアネート、m-キシリレンジイソシアネート、p-キシリレンジイソシアネート、ナフタレン-2,6-ジイソシアネート、4,4’-(2,2ビス(4-フェノキシフェニル)プロパン)ジイソシアネート、3,3’-または2,2’-ジメチルビフェニル-4,4’-ジイソシアネート、3,3’-または2,2’-ジエチルビフェニル-4,4’-ジイソシアネート、3,3’-ジメトキシビフェニル-4,4’-ジイソシアネート、3,3’-ジエトキシビフェニル-4,4’-ジイソシアネートなどの芳香族ジイソシアネート類、及びこれらのいずれかを水素添加したジイソシアネート(例えば、イソホロンジイソシアネート、1,4-シクロヘキサンジイソシアネート、1,3-シクロヘキサンジイソシアネート、4,4’-ジシクロヘキシルメタンジイソシアネート、ヘキサメチレンジイソシアネート)などが挙げられる。これらの中では、低吸湿性、寸法安定性、価格及び重合性の点からジフェニルメタン-4,4’-ジイソシアネート、トリレン-2,4-ジイソシアネート、トリレン-2,6-ジイソシアネート、3,3’-ジメチルビフェニル-4,4’-ジイソシアネートやナフタレン-2,6-ジイソシアネート、4,4’-ジシクロヘキシルメタンジイソシアネート、1,4-シクロヘキサンジイソシアネートが好ましい。尚、ジイソシアネート類は単独で使用してもよいし複数を組み合わせて使用してもよい。 Examples of diisocyanates include diphenylmethane-2,4'-diisocyanate, 3,2'- or 3,3'- or 4,2'- or 4,3'- or 5,2'- or 5,3' - or 6,2'- or 6,3'-dimethyldiphenylmethane-2,4'-diisocyanate, 3,2'- or 3,3'- or 4,2'- or 4,3'- or 5,2 '-or 5,3'-or 6,2'-or 6,3'-diethyldiphenylmethane-2,4'-diisocyanate, 3,2'-or 3,3'-or 4,2'-or 4, 3'- or 5,2'- or 5,3'- or 6,2'- or 6,3'-dimethoxydiphenylmethane-2,4'-diisocyanate, diphenylmethane-4,4'-diisocyanate, diphenylmethane-3, 3'-diisocyanate, diphenylmethane-3,4'-diisocyanate, diphenyl ether-4,4'-diisocyanate, benzophenone-4,4'-diisocyanate, diphenylsulfone-4,4'-diisocyanate, tolylene-2,4-diisocyanate, Tolylene-2,6-diisocyanate, m-xylylene diisocyanate, p-xylylene diisocyanate, naphthalene-2,6-diisocyanate, 4,4'-(2,2bis(4-phenoxyphenyl)propane) diisocyanate, 3, 3'- or 2,2'-dimethylbiphenyl-4,4'-diisocyanate, 3,3'- or 2,2'-diethylbiphenyl-4,4'-diisocyanate, 3,3'-dimethoxybiphenyl-4, Aromatic diisocyanates such as 4'-diisocyanate, 3,3'-diethoxybiphenyl-4,4'-diisocyanate, and diisocyanates obtained by hydrogenating any of these (e.g., isophorone diisocyanate, 1,4-cyclohexane diisocyanate, 1,3-cyclohexane diisocyanate, 4,4'-dicyclohexylmethane diisocyanate, hexamethylene diisocyanate) and the like. Among these, diphenylmethane-4,4'-diisocyanate, tolylene-2,4-diisocyanate, tolylene-2,6-diisocyanate, 3,3'- Dimethylbiphenyl-4,4'-diisocyanate, naphthalene-2,6-diisocyanate, 4,4'-dicyclohexylmethane diisocyanate, and 1,4-cyclohexane diisocyanate are preferred. Note that the diisocyanates may be used alone or in combination.
 前記溶媒としては、ポリイミド或いはポリイミドの前駆体を溶解可能であればよく、非プロトン性極性溶媒などを好適に用いることができる。例えば、N,N-ジメチルホルムアミド、N,N-ジメチルアセトアミド、N,N-ジエチルアセトアミド、N,N-ジメチルメトキシアセトアミドなどのN,N-ジ低級アルキルカルボキシルアミド類、N-メチル-2-ピロリドン、N-エチル-2-ピロリドン、ジメチルスルホキシド、ジメチルスルホン、1,3-ジメチル-2-イミダゾリジノン、γ-ブチロラクトン、ジグライム、m-クレゾール、ヘキサメチルホスホルアミド、N-アセチル-2-ピロリドン、ヘキサメチルホスホルアミド、エチルセロソルブアセテート、ジエチレングリコールジメチルエーテル、スルホラン、p-クロロフェノールなどが挙げられる。なお、溶媒は2種以上の混合物であってもよい。 The solvent may be any solvent as long as it can dissolve polyimide or a precursor of polyimide, and aprotic polar solvents and the like can be suitably used. For example, N,N-dilower alkylcarboxylamides such as N,N-dimethylformamide, N,N-dimethylacetamide, N,N-diethylacetamide, N,N-dimethylmethoxyacetamide, N-methyl-2-pyrrolidone , N-ethyl-2-pyrrolidone, dimethylsulfoxide, dimethylsulfone, 1,3-dimethyl-2-imidazolidinone, γ-butyrolactone, diglyme, m-cresol, hexamethylphosphoramide, N-acetyl-2-pyrrolidone , hexamethylphosphoramide, ethyl cellosolve acetate, diethylene glycol dimethyl ether, sulfolane, p-chlorophenol and the like. Note that the solvent may be a mixture of two or more kinds.
 前記フィルムの厚さは3μm以上が好ましく、より好ましくは7μm以上であり、さらに好ましくは14μm以上であり、より一層好ましくは20μm以上である。前記フィルムの厚さの上限は特に制限されないが、フレキシブル電子デバイスとして用いるためには250μm以下であることが好ましく、より好ましくは100μm以下であり、さらに好ましくは50μm以下である。 The thickness of the film is preferably 3 μm or more, more preferably 7 μm or more, even more preferably 14 μm or more, and even more preferably 20 μm or more. The upper limit of the thickness of the film is not particularly limited, but in order to use it as a flexible electronic device, it is preferably 250 μm or less, more preferably 100 μm or less, and still more preferably 50 μm or less.
 前記フィルムが、透明ポリイミドフィルムである場合、その黄色度指数(以下、「イエローインデックス」または「YI」ともいう。)は10以下が好ましく、より好ましくは7以下であり、さらに好ましくは5以下であり、より一層好ましくは3以下である。前記透明ポリイミドの黄色度指数の下限は特に制限されないが、フレキシブル電子デバイスとして用いるためには0.1以上であることが好ましく、より好ましくは0.2以上であり、さらに好ましくは0.3以上である。 When the film is a transparent polyimide film, its yellowness index (hereinafter also referred to as "yellow index" or "YI") is preferably 10 or less, more preferably 7 or less, and still more preferably 5 or less. Yes, and even more preferably 3 or less. The lower limit of the yellowness index of the transparent polyimide is not particularly limited, but in order to use it as a flexible electronic device, it is preferably 0.1 or more, more preferably 0.2 or more, and still more preferably 0.3 or more. It is.
 前記フィルムは、その製造時において幅が300mm以上、長さが10m以上の長尺フィルムとして巻き取られた形態で得られるものが好ましく、巻取りコアに巻き取られたロール状フィルムの形態のものがより好ましい。前記フィルムがロール状に巻かれていると、ロール状に巻かれたフィルムという形態での輸送が容易となる。 The film is preferably obtained in the form of a rolled film having a width of 300 mm or more and a length of 10 m or more at the time of manufacture, and is in the form of a rolled film wound around a winding core. is more preferable. When the film is wound into a roll, it becomes easy to transport the film in the form of a roll.
 前記フィルムにおいては、ハンドリング性および生産性を確保する為、フィルム中に粒子径が10~1000nm程度の滑剤(粒子)を、0.03~3質量%程度、添加・含有させて、フィルム表面に微細な凹凸を付与して滑り性を確保することが好ましい。滑剤の粒子径は好ましくは20~500nmであり、より好ましくは30~300nmであり、さらに好ましくは50~200nmである。滑剤の粒子径を10nm以上とすることで添加量に対して十分な滑り性を発現することができる。また、滑剤の粒子径を1000nm以下とすることで機械強度の低下や、フィルムの白濁などの問題を低減させることができる。 In the above film, in order to ensure ease of handling and productivity, approximately 0.03 to 3% by mass of lubricant (particles) with a particle size of approximately 10 to 1000 nm is added to the film surface. It is preferable to provide fine irregularities to ensure slipperiness. The particle size of the lubricant is preferably 20 to 500 nm, more preferably 30 to 300 nm, and even more preferably 50 to 200 nm. By setting the particle size of the lubricant to 10 nm or more, sufficient slipperiness can be achieved with respect to the amount added. Furthermore, by setting the particle size of the lubricant to 1000 nm or less, problems such as a decrease in mechanical strength and clouding of the film can be reduced.
 本発明のフィルムの製造装置は、
 熱処理前フィルムの一方の面の幅方向の両端部に固定具を設置し、前記固定具で前記熱処理フィルムを固定する固定機構A
 前記熱処理前フィルムの両面に熱風を送風する送風機構B
 前記熱処理前フィルムを搬送する搬送機構C
 を有し、
 前記送風機構Bは、固定具を設置していない面に送風する熱風の風速が、固定具を設置している面に送風する熱風の風速と、同じかそれよりも大きいことを特徴とする製造装置である。
 前記前記製造装置におけるフィルムおよび機構A~Cは、フィルムの製造方法で説明した内容と同義である。
The film manufacturing apparatus of the present invention includes:
A fixing mechanism A in which fixing tools are installed at both ends in the width direction of one surface of the film before heat treatment, and the heat treated film is fixed with the fixing tools.
Blowing mechanism B blowing hot air to both sides of the film before heat treatment
Conveyance mechanism C that conveys the film before heat treatment
has
The blowing mechanism B is manufactured in such a manner that the speed of hot air blown to a surface where no fixture is installed is the same as or higher than the speed of hot air blown to a surface where a fixture is installed. It is a device.
The film and mechanisms A to C in the manufacturing apparatus have the same meaning as described in the film manufacturing method.
 以下、本発明に関し実施例を用いて詳細に説明するが、本発明はその要旨を超えない限り、以下の実施例に限定されるものではない。 Hereinafter, the present invention will be explained in detail using Examples, but the present invention is not limited to the following Examples unless it exceeds the gist thereof.
<合成例1(ポリアミド酸溶液Aの調製)>
 窒素導入管、還流管、攪拌棒を備えた反応容器内を窒素置換した後、33.36質量部の4,4’-ジアミノ-2,2’-ビス(トリフルオロメチル)ビフェニル(TFMB)、270.37質量部のN,N-ジメチルアセトアミド(DMAC)とコロイダルシリカをジメチルアセトアミドに分散してなる分散体(日産化学工業製「スノーテックス(登録商標)DMAC-ST」)とをシリカがポリアミド酸溶液中のポリマー固形分総量にて0.15質量%になるように加え完全に溶解させ、次いで、9.81質量部の1,2,3,4-シクロブタンテトラカルボン酸二無水物(CBDA)、11.34質量部の3,3’,4,4’-ビフェニルテトラカルボン酸二無水物(BPDA)、4.85質量部の4,4’-オキシジフタル酸無二水物(ODPA)を固体のまま分割添加した後、室温で24時間攪拌した。その後、165.7質量部のDMAcを加え希釈し、固形分18質量%、還元粘度2.7dl/gのポリアミド酸溶液A(PAA-A)(TFMB//CBDA/BPDA/ODPAのモル比=1.00//0.48/0.37/0.15)を得た。
<Synthesis Example 1 (Preparation of polyamic acid solution A)>
After replacing the inside of the reaction vessel equipped with a nitrogen introduction tube, a reflux tube, and a stirring bar with nitrogen, 33.36 parts by mass of 4,4'-diamino-2,2'-bis(trifluoromethyl)biphenyl (TFMB), A dispersion of 270.37 parts by mass of N,N-dimethylacetamide (DMAC) and colloidal silica dispersed in dimethylacetamide ("Snowtex (registered trademark) DMAC-ST" manufactured by Nissan Chemical Industries) was prepared by dispersing silica into polyamide. The total amount of polymer solids in the acid solution was added to be 0.15% by mass and completely dissolved, and then 9.81 parts by mass of 1,2,3,4-cyclobutanetetracarboxylic dianhydride (CBDA ), 11.34 parts by mass of 3,3',4,4'-biphenyltetracarboxylic dianhydride (BPDA), and 4.85 parts by mass of 4,4'-oxydiphthalic anhydride (ODPA). After adding the solid in portions, the mixture was stirred at room temperature for 24 hours. Thereafter, 165.7 parts by mass of DMAc was added and diluted to form a polyamic acid solution A (PAA-A) with a solid content of 18 mass% and a reduced viscosity of 2.7 dl/g (TFMB//molar ratio of CBDA/BPDA/ODPA= 1.00//0.48/0.37/0.15).
<合成例2(ポリアミド酸溶液Bの調製)>
 窒素導入管、撹拌翼を備えた反応器に窒素を通過させながらピロメリット酸二無水物(PMDA)3.16質量部、3,3’,4,4’-ビフェニルテトラカルボン酸二無水物(BPDA)2.84質量部、4,4’-ジアミノ-2,2’-ビス(トリフルオロメチル)ビフェニル(TFMB)7.73質量部を入れ、N,N-ジメチルアセトアミド(DMAc、77.8質量部)、コロイダルシリカ(滑剤)をジメチルアセトアミドに分散してなる分散体(日産化学工業製「スノーテックス(登録商標)DMAC-ST-ZL」)とを、コロイダルシリカ(滑剤)がポリアミド酸溶液中のポリマー固形分総量に対して0.15質量%になるように加えた後、25℃下24時間撹拌することでポリアミド酸溶液B(PAA-B)(TFMB//PMDA/BPDA)を得た。
<Synthesis Example 2 (Preparation of polyamic acid solution B)>
While passing nitrogen through a reactor equipped with a nitrogen introduction tube and a stirring blade, 3.16 parts by mass of pyromellitic dianhydride (PMDA) and 3,3',4,4'-biphenyltetracarboxylic dianhydride ( Add 2.84 parts by mass of BPDA), 7.73 parts by mass of 4,4'-diamino-2,2'-bis(trifluoromethyl)biphenyl (TFMB), and add N,N-dimethylacetamide (DMAc, 77.8 parts by mass). Parts by mass), a dispersion of colloidal silica (lubricant) dispersed in dimethylacetamide (Snowtex (registered trademark) DMAC-ST-ZL, manufactured by Nissan Chemical Industries), colloidal silica (lubricant) dispersed in polyamic acid solution Polyamic acid solution B (PAA-B) (TFMB//PMDA/BPDA) was obtained by adding it to 0.15% by mass based on the total polymer solid content and stirring at 25°C for 24 hours. Ta.
 実施例1
 得られたポリアミド酸溶液Aを、コンマコーターを用いてポリエチレンテレフタレート製フィルムA4100(東洋紡株式会社製)の無滑材面上に最終膜厚が20μmとなるよう塗布した。これを90℃にて15分間乾燥した。乾燥後に自己支持性を得たポリアミド酸フィルムを支持体としてきたA4100フィルムから剥離し、ポリアミド酸フィルム(熱処理前フィルム)を得た。次いで、熱処理前フィルムの下側の面の端部にピンテンター11(フィルム固定具)をピン11a(フィルム固定構造)が上向きになるよう設置し、熱処理前フィルム端部をピンに差し込むことにより固定した。次いで、熱処理前フィルムが破断しないように、ピンシート間隔を調整して搬送し、上部吹出口から固定具非設置面に、および、下部吹出口から固定具設置面に、それぞれ250℃で3分、290℃で3分、340℃で3分、350℃で3分の条件で熱風を送風して加熱し、イミド化反応を進行させた。この時、それぞれの温度ゾーンにおいて熱処理前フィルムの通過位置に対して上下175mm離れた場所に熱風吹出口を設置し、この上部吹出口(フィルムの固定具非設置面方向)から風速3.8m/秒となる熱風を、下部吹出口(フィルムの固定具設置面方向)から3.6m/秒となる熱風を供給した。その後、2分間で室温にまで冷却し、フィルムの両端の平面性が悪い部分をスリッターにて切り落とし、ロール状に巻き上げ、幅500mmのポリイミドフィルムを100m得た。
Example 1
The obtained polyamic acid solution A was applied onto the non-slip surface of polyethylene terephthalate film A4100 (manufactured by Toyobo Co., Ltd.) using a comma coater so that the final film thickness was 20 μm. This was dried at 90°C for 15 minutes. The polyamic acid film that had obtained self-supporting properties after drying was peeled off from the A4100 film used as a support to obtain a polyamic acid film (film before heat treatment). Next, a pin tenter 11 (film fixing device) was installed at the end of the lower surface of the film before heat treatment so that the pin 11a (film fixing structure) faced upward, and the end of the film before heat treatment was fixed by inserting it into the pin. . Next, the pin sheet interval was adjusted so that the film before heat treatment would not break, and the film was conveyed at 250°C for 3 minutes from the upper air outlet to the surface where the fixture was not installed, and from the lower air outlet to the surface where the fixture was installed. , 3 minutes at 290° C., 3 minutes at 340° C., and 3 minutes at 350° C. by blowing hot air to advance the imidization reaction. At this time, a hot air outlet was installed at a location 175 mm above and below the passing position of the film before heat treatment in each temperature zone, and the air velocity was 3.8 m/min from this upper outlet (in the direction of the surface where the film fixing device was not installed). Hot air at a velocity of 3.6 m/sec was supplied from the lower outlet (in the direction of the film fixture installation surface). Thereafter, the film was cooled to room temperature for 2 minutes, and portions with poor flatness at both ends of the film were cut off using a slitter, and rolled up into a roll to obtain 100 m of polyimide film with a width of 500 mm.
 実施例2~4
 使用した樹脂、製造条件を表1のとおりとし、実施例1と同様に操作し、それぞれポリイミドフィルムを得た。
Examples 2-4
The resins used and the manufacturing conditions were as shown in Table 1, and the same procedures as in Example 1 were performed to obtain polyimide films.
 比較例1~2
 使用した樹脂、製造条件を表1のとおりとし、実施例1と同様に操作し、それぞれポリイミドフィルムを得た。
Comparative examples 1-2
The resins used and the manufacturing conditions were as shown in Table 1, and the same procedures as in Example 1 were performed to obtain polyimide films.
<吹出口風速測定>
 室温状態の熱処理炉にて室温の風を送り込む状態に設定し、熱風吹出口にて風速計(カノマックス:ANEMOMASTER:MODEL6003)を用いて、測定した。
<Outlet wind speed measurement>
A heat treatment furnace at room temperature was set to send air at room temperature, and measurement was performed using an anemometer (ANEMOMASTER: MODEL 6003) at the hot air outlet.
<フィルム外観(端部)>
 炉内搬送中の熱処理前フィルムの状態、および、熱処理後のフィルム端部(固定部)の状態を目視にて確認し評価した。評価は下記の三段階で行った。
 〇:フィルム搬送に問題なく、フィルムが適切に張られた状態を維持できる
 △:フィルム搬送に問題はないが、フィルムが適切に張られた状態を維持できない
 ×:破断や裂けによって分離もしくは垂れ下がったフィルムが炉内壁面等に接触し、搬送不可
<Film appearance (edge)>
The state of the film before heat treatment during transport in the furnace and the state of the end portion (fixed portion) of the film after heat treatment were visually checked and evaluated. Evaluation was performed in the following three stages.
〇: There is no problem with film transport, and the film can be maintained properly stretched. △: There is no problem with film transport, but the film cannot be maintained properly stretched. ×: Separated or hanging due to breakage or tearing. The film comes into contact with the inner wall of the furnace and cannot be transported.
<フィルム外観(中央部)>
 破断や裂け、シワ等の異常がないか、固定部をカットした残り部分全体を目視にて評価した。評価は下記の二段階で行った。
 〇:フィルム端部(固定部)を除いた何れにも、破断や裂け、シワ等の異常がない
 ×:フィルム端部(固定部)を除いた何れかに、破断や裂け、シワ等の異常がみられる
<Film appearance (center)>
The entire remaining portion after cutting the fixed portion was visually evaluated for abnormalities such as breaks, tears, and wrinkles. The evaluation was performed in the following two stages.
〇: There is no abnormality such as breakage, tearing, wrinkles, etc. in any part other than the film end (fixed part) ×: There is no abnormality such as breakage, tear, wrinkle, etc. in any part other than the film end (fixed part) can be seen
<全光線透過率>
 HAZEMETER(NDH5000、日本電色社製)を用いてフィルムの全光線透過率(TT)を測定した。光源としてはD65ランプを使用した。ロール状に巻き上げたフィルムから2m巻き出して50mm□のフィルムを5枚切り出し、それぞれのフィルムについて1回の測定を行うことによって得られる計5点の測定値の算術平均値を採用した。
<Total light transmittance>
The total light transmittance (TT) of the film was measured using HAZEMETER (NDH5000, manufactured by Nippon Denshoku Co., Ltd.). A D65 lamp was used as a light source. The arithmetic mean value of the five measured values obtained by unwinding a roll of film by 2 m, cutting out five 50 mm square films, and performing one measurement on each film was used.
<膜厚>
 フィルムの膜厚を、フィルム厚さ測定器HKT-1216(マール社製)を用いて測定した。ロール状に巻き上げたフィルムから2.5m巻き出し、フィルムの任意の一端から内側に2cm間隔で全幅測定し、その平均をフィルムの膜厚とした。
<Film thickness>
The thickness of the film was measured using a film thickness measuring device HKT-1216 (manufactured by Marl Corporation). The film was rolled up into a roll, and the film was unwound by 2.5 m, and the full width was measured at 2 cm intervals inward from any one end of the film, and the average of the measurements was taken as the thickness of the film.
<YI>
 カラーメーター(ZE6000、日本電色社製)およびC2光源を使用して、ASTM D1925に準じてフィルムの三刺激値XYZ値を測定し、下記式により黄色度指数(YI)を算出した。ロール状に巻き上げたフィルムから3m巻き出して50mm□のフィルムを5枚切り出し、それぞれのフィルムについて1回の測定を行うことによって得られる計5点の測定値の算術平均値を採用した。
YI=100×(1.28X-1.06Z)/Y
<YI>
Using a color meter (ZE6000, manufactured by Nippon Denshoku Co., Ltd.) and a C2 light source, the tristimulus XYZ values of the film were measured according to ASTM D1925, and the yellowness index (YI) was calculated using the following formula. The arithmetic mean value of the five measured values obtained by unwinding a roll of film by 3 m, cutting out five 50 mm square films, and performing one measurement on each film was used.
YI=100×(1.28X-1.06Z)/Y
<Tg(ガラス転移温度)>
 ガラス転移温度は、ロール状に巻き上げたフィルムから3.5m巻き出したところの幅方向中心部分から5mm×20mmのサイズのフィルムを1枚切り出し、動的粘弾性測定装置(TAインスツルメンツ社製DMA Q800)を用いて、30℃から450℃まで昇温速度5℃/分、周波数10Hzで測定を行い、弾性率変化(機械的tanδ)が最大となる温度をガラス転移温度とした。詳細な測定条件は下記の通り。
測定モード:DMA Multi-Frequency-strain Tenshio
n film/Rectangular
strain:0.1%
Preload force:0.02N
Force track:125%
Poisson‘s ratio:0.440
<Tg (glass transition temperature)>
The glass transition temperature was determined by cutting out a sheet of 5 mm x 20 mm from the center of the width of a 3.5 m roll of film, and using a dynamic viscoelasticity measuring device (DMA Q800 manufactured by TA Instruments). ), measurement was performed from 30° C. to 450° C. at a heating rate of 5° C./min and a frequency of 10 Hz, and the temperature at which the change in elastic modulus (mechanical tan δ) was maximum was defined as the glass transition temperature. Detailed measurement conditions are as follows.
Measurement mode: DMA Multi-Frequency-strain Tenshio
n film/Rectangular
Strain: 0.1%
Preload force: 0.02N
Force track: 125%
Poisson's ratio: 0.440
<CTE(線熱膨張係数)>
 ロール状に巻き上げたフィルムから4m巻き出したところの幅方向中心部分から塗布時の流れ方向(MD方向)を長辺とする20mm×2mmのサイズのフィルムを1枚と幅方向(TD方向)を長辺とする20mm×2mmのサイズのフィルムを1枚とを切り出し、各々において下記条件にて伸縮率を測定し、30℃~45℃、45℃~60℃のように15℃の間隔での伸縮率/温度を測定し、この測定を300℃まで行い、全測定値の平均値をCTEとして算出し、さらにMD方向を長辺とするフィルムにおける算出結果とTD方向を長辺とするフィルムにおける算出結果の平均値を求めた。
  機器名    ; MACサイエンス社製TMA4000S
  試料長さ   ; 20mm
  試料幅    ; 2mm
  昇温開始温度 ; 25℃
  昇温終了温度 ; 300℃
  昇温速度   ; 5℃/min
  雰囲気    ; アルゴン
<CTE (coefficient of linear thermal expansion)>
One film of size 20mm x 2mm with the long side in the flow direction (MD direction) at the time of coating and one film in the width direction (TD direction) from the center part in the width direction after unwinding 4m from the rolled film. Cut out one piece of film with a size of 20 mm x 2 mm as the long side, and measure the expansion and contraction rate of each film under the following conditions. Measure the expansion/contraction rate/temperature, perform this measurement up to 300°C, calculate the average value of all measured values as CTE, and further compare the calculation results for the film whose long side is in the MD direction and the calculation result for the film whose long side is in the TD direction. The average value of the calculation results was determined.
Equipment name: TMA4000S manufactured by MAC Science
Sample length: 20mm
Sample width: 2mm
Heating start temperature: 25℃
Heating end temperature: 300℃
Temperature increase rate: 5℃/min
Atmosphere: argon
 上記の実施例および比較例で得られたフィルムについて、フィルム外観(中央部および端部)、YI、Tg、CTEについて評価した結果を下記表1に示す。 The films obtained in the above Examples and Comparative Examples were evaluated in terms of film appearance (center and edges), YI, Tg, and CTE, and the results are shown in Table 1 below.
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001
 本発明は、フィルムの製造において、フィルム中央部のみならず、フィルムを固定した両端部やその付近にも破断や裂け、外観異常が生じないフィルムを提供することができ、例えばフレキシブル電子デバイスに好ましく適用できる。 INDUSTRIAL APPLICABILITY The present invention can provide a film that does not cause breakage, tearing, or abnormal appearance not only at the center of the film but also at and around both ends where the film is fixed, and is suitable for, for example, flexible electronic devices. Applicable.
 1   フィルム(熱処理前フィルム)
 1a  フィルム中央部
 1b  フィルム端部
 11  ピンシート(フィルム固定具)
 11a ピン(フィルム固定構造)
 21  フィルム固定具が設置されていない面側の熱風吹出口
 22  フィルム固定具が設置されている面側の熱風吹出口
 31  フィルム固定具が設置されていない面側に吹きつける熱風
 32  フィルム固定具が設置されている面側に吹きつける熱風
1 Film (film before heat treatment)
1a Film center part 1b Film end part 11 Pin sheet (film fixing tool)
11a Pin (film fixing structure)
21 Hot air outlet on the side where the film fixing device is not installed 22 Hot air outlet on the side where the film fixing device is installed 31 Hot air blowing on the side where the film fixing device is not installed 32 Hot air outlet on the side where the film fixing device is installed Hot air blowing on the surface where it is installed

Claims (6)

  1.  フィルムの製造方法であって、
     熱処理前フィルムの一方の面の幅方向の両端部に固定具を設置し、前記固定具で前記熱
    処理フィルムを固定する工程A
     前記熱処理前フィルムの両面に熱風を送風する工程B
     前記熱処理前フィルムを搬送する工程C
     を有し、
     前記工程Bは、固定具を設置していない面に送風する熱風の風速が、固定具を設置している面に送風する熱風の風速と、同じかそれよりも大きいことを特徴とするフィルムの製造方法。
    A method for producing a film, the method comprising:
    Step A of installing fixtures at both ends in the width direction of one side of the film before heat treatment, and fixing the heat treated film with the fixtures;
    Step B of blowing hot air onto both sides of the film before heat treatment
    Step C of conveying the film before heat treatment
    has
    The process B is characterized in that the speed of the hot air blown to the surface where the fixing device is not installed is the same as or higher than the speed of the hot air blown to the surface where the fixing device is installed. Production method.
  2.  前記工程Bは、前記固定具を設置していない面の風速が、前記固定具を設置している面の風速の1.0倍超である請求項1に記載のフィルムの製造方法。 The method for producing a film according to claim 1, wherein in the step B, the wind speed on the surface where the fixing device is not installed is more than 1.0 times the wind speed on the surface where the fixing device is installed.
  3.  前記固定具がピンシートである請求項1または2に記載のフィルムの製造方法。 The method for producing a film according to claim 1 or 2, wherein the fixture is a pin sheet.
  4.  前記フィルムがポリイミドフィルムである請求項1または2に記載のフィルムの製造方法。 The method for producing a film according to claim 1 or 2, wherein the film is a polyimide film.
  5.  前記ポリイミドフィルムが透明ポリイミドフィルムである請求項4に記載のフィルムの製造方法。 The method for producing a film according to claim 4, wherein the polyimide film is a transparent polyimide film.
  6.  フィルムの製造装置であって、
     熱処理前フィルムの一方の面の幅方向の両端部に固定具を設置し、前記固定具で前記熱処理フィルムを固定する固定機構A
     前記熱処理前フィルムの両面に熱風を送風する送風機構B
     前記熱処理前フィルムを搬送する搬送機構C
     を有し、
     前記送風機構Bは、固定具を設置していない面に送風する熱風の風速が、固定具を設置している面に送風する熱風の風速と、同じかそれよりも大きいことを特徴とするフィルムの製造装置。
    A film manufacturing device,
    A fixing mechanism A in which fixing tools are installed at both ends in the width direction of one surface of the film before heat treatment, and the heat treated film is fixed with the fixing tools.
    Blowing mechanism B blowing hot air to both sides of the film before heat treatment
    Conveyance mechanism C that conveys the film before heat treatment
    has
    The blowing mechanism B is a film characterized in that the speed of the hot air blown to the surface where the fixing device is not installed is the same as or higher than the speed of the hot air blown to the surface where the fixing device is installed. manufacturing equipment.
PCT/JP2023/022937 2022-06-23 2023-06-21 Method for producing film WO2023249053A1 (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0596619A (en) * 1991-10-08 1993-04-20 Mitsubishi Heavy Ind Ltd Film stretching machine
JP2006346929A (en) * 2005-06-14 2006-12-28 Toyobo Co Ltd Manufacturing apparatus of polymer film and manufacturing method of polymer film
JP2011183724A (en) * 2010-03-10 2011-09-22 Fujifilm Corp Tentering machine, method for eliminating foreign substance in tentering machine and solution film forming equipment
JP2019090843A (en) * 2016-03-31 2019-06-13 コニカミノルタ株式会社 Method for manufacturing optical film

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0596619A (en) * 1991-10-08 1993-04-20 Mitsubishi Heavy Ind Ltd Film stretching machine
JP2006346929A (en) * 2005-06-14 2006-12-28 Toyobo Co Ltd Manufacturing apparatus of polymer film and manufacturing method of polymer film
JP2011183724A (en) * 2010-03-10 2011-09-22 Fujifilm Corp Tentering machine, method for eliminating foreign substance in tentering machine and solution film forming equipment
JP2019090843A (en) * 2016-03-31 2019-06-13 コニカミノルタ株式会社 Method for manufacturing optical film

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