JP2006306555A - Device and method for manufacturing polymer film - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a manufacturing device suitable for manufacturing a polymer film, and a manufacturing method for manufacturing the polymer film using the device, capable of suppressing a problem that the film is broken in a long hole shape in the width direction of the film at a hole with a pin bitten therein when the polymer film, in particular, a polyimide film is manufactured, and the drying and the heat treatment are performed by using a tenter type conveying device. <P>SOLUTION: In the polymer film manufacturing device, and the polymer film manufacturing method using the same, the polymer film manufacturing device having a tenter treatment unit has a means of cooling the polymer film, or a film consisting of its precursor so that the temperature of a pin is below 180°C at the film holding starting point at which the pin pierces both ends of the film and carries the film. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  The present invention relates to an apparatus for producing a polymer film. In particular, a tenter-type (film transport) treatment in producing a polymer film by subjecting a precursor film to a high-temperature heat treatment at the time of a final heat treatment in producing the polymer film. The present invention relates to an apparatus for producing a polymer film having a feature in a part, and also relates to a method for producing a polymer film using the apparatus.

When a polyimide film is produced, an undried precursor film (green film) is imidized at a high temperature. In this case, the undried precursor film is heat-treated while being transported and dried and heat-treated. The retained film and precursor film are generally dried and thus shrink. In such film transport / drying / heat treatment, as an apparatus for manufacturing a film by transporting the film in the stretched width direction by holding both ends in the width direction of the film with a number of pins and clips, A tenter type conveying device for a film (sheet) called a so-called tenter is known (see Patent Document 1).
In addition, it is also known to use a tenter type conveying device for manufacturing a polyimide film (see Patent Document 2).
Japanese Examined Patent Publication No. 39-029211. JP 09-188863 A

The film conveying apparatus has been well known for a long time to be used for drying so as not to cause wrinkles in the drying process after dyeing the cloth. In addition to drying the cloth, it is also used for drying an undried plastic film by a solvent film forming method while transporting it in a drying process. By using the film conveying device, it is possible to prevent the film from shrinking in the width direction due to heat during drying and heat treatment, and to prevent wrinkles due to shrinkage from occurring in the film after drying and heat treatment.
The shrinkage of the film occurs not only in the width direction of the film but in all directions. However, the transporting tension acts in the transport direction of the film and has an effect of suppressing the shrinkage. Thus, the strength and flatness required for the dried and heat-treated film can be ensured by transporting the undried film using the tenter type transport device when drying and heat-treating the film.

  Among the film tenter type conveying devices, the tenter type conveying device for the film that holds the film stretched in the width direction by biting a large number of pins along both side edges of the film was arranged in parallel A large number of pins are arranged on a pin sheet supported in a row by a pair of moving chains. This film tenter type transport device is simpler in structure than the film transport device such as the clip, or can be structured to reverse the transport conveyor path in the drying chamber. On the other hand, since the fine pieces of the film generate dust when the pins are bitten into the film, it is necessary to reduce the number of pins as much as possible. Moreover, when the shrinkage force of a film becomes large, the hole which pinched the pin into the film surface has the subject that it breaks into a long hole shape in the width direction of a film.

In order to improve these, a method has also been proposed in which a film having a high tear strength is additionally stacked for reinforcement at the gripping portion of the film pin (see Patent Document 3).
Furthermore, a tenter type conveying device has also been proposed in which the innermost pin density is increased and the outer pin arrangement density is further reduced in the arrangement of pins that can be placed on both ends of the web when the web is conveyed (patent). Reference 4). Even in these proposals for improvement, there is nothing to consider the arrangement in the conveying direction of the pins, particularly the arrangement of the pins between the pin sheets. There was a problem in the production of films that are likely to occur.
Conventional tenter type transport devices for films tend to cause production loss due to problems such as breakage in the shape of a long hole in the width direction of the film at the hole where the pin is entrapped, and generation of wrinkles. At the same time, the production efficiency was lowered, and it was not satisfactory for users.
JP-A-11-254521 Japanese Patent Application Laid-Open No. 09-073315

  The present invention has a problem that, when a polyimide film is produced, when a drying or heat treatment is carried out using a tenter type conveying device, the film breaks into a long hole in the width direction of the film at the hole in which the pin is bitten. An object of the present invention is to provide a production apparatus suitable for production of a polymer film capable of suppressing the above and a method for producing a polymer film produced using the apparatus.

As a result of intensive studies, the present inventors have determined that when a polymer film such as a polyimide film is dried or heat-treated using a tenter type conveying device, the film is conveyed by gripping both side edges of the film with pins. By devising the arrangement of the above, it has been found that it is possible to suppress the problem of breaking into a long hole outward in the width direction of the film in the hole in which the pin has been entrapped, and a polymer film production apparatus suitable for polymer film production Created.
That is, this invention consists of the following structures.
1. When a film made of a polymer film or a precursor thereof is subjected to a heat treatment or the like with a film end fixed tenter, the film end gripping at both end portions in the width direction of the film is performed individually with a large number of pin sheets. A high-tensile processing unit that transports the film in a state where the film is stretched in the width direction and / or the transport direction. In the molecular film manufacturing apparatus, it has a means to cool so that the temperature of a pin may be less than 180 degreeC when this pin stabs and conveys both ends of a film, and it has a means to cool.
2. When a film made of a polymer film or a precursor thereof is subjected to a heat treatment or the like with a film end fixed tenter, the film end gripping at both end portions in the width direction of the film is performed individually with a large number of pin sheets. A high-tensile processing unit that transports the film in a state where the film is stretched in the width direction and / or the transport direction. When a polymer film is produced using a molecular film production apparatus, the pin is cooled so that the temperature of the pin becomes less than 180 ° C. when the pin is pierced and conveyed at both ends of the film. A method for producing a film.

  The polymer film manufacturing apparatus of the present invention is a tenter type processing unit (conveying device) for a polymer film such as a polyimide film, while the pin sheets on both sides of the film are running in parallel with the pin sheets on the opposite side. When the film grips the film, the film is cooled to less than 180 ° C., so that deformation of the film is suppressed at the film gripping part, and the film is mainly elongated in the width direction at the hole where the pin is bitten Breaking into a hole is suppressed, and as a result, it is possible to achieve a reduction in distortion and a reduction in film thickness variation throughout the film. The pin part is easy to tear, and when it is torn, film fragments are scattered in the pin tenter, and the environment is damaged and a high-quality film can be obtained. High-quality polyimide film and other polymer films can be easily obtained and contribute to the productivity of polymer film production. This is an extremely effective industrial method.

In the present invention, the polymer film includes a film made of a high melting point or non-melting polymer such as polyamideimide, polyimide, cellulose acetate, polycarbonate, polyvinyl chloride, and aramid.
The polymer film of the present invention is cast into a film by casting a solution containing these polymers, drying and heat treatment. Examples of the solvent used for the solution containing these polymers include N-methyl-2-pyrrolidone, N, N-dimethylformamide, N, N-dimethylacetamide, methylene chloride, tetrahydrofuran, methanol, and metacresol.
Examples of the polymer solution preferably used in the present invention include N-methyl-2-pyrrolidone solution of polyamideimide, N, N-dimethylacetamide solution, N-methyl-2-pyrrolidone solution of polyamide acid which is a polyimide precursor, N , N-dimethylacetamide solution, N-methyl-2-pyrrolidone solution of solvent-soluble polyimide, N, N-dimethylacetamide solution, methylene chloride solution of cellulose acetate, methanol solution, methylene chloride solution of polycarbonate, metacresol solution, Examples include a tetrahydrofuran solution of polyvinyl chloride and an N-methyl-2-pyrrolidone solution of aramid.

The polymer film production apparatus and production method of the present invention are particularly suitable for polyamic acid which is a precursor of a polyamic acid which is a polyimide precursor, an N-methyl-2-pyrrolidone solution, an N, N-dimethylacetamide solution or a polyimide benzoxazole. The present invention can be most preferably applied by the casting film forming method using a solution of N-methyl-2-pyrrolidone, N, N-dimethylformamide, N, N-dimethylacetamide, or the like. Hereinafter, the polyimide film will be described in detail, but is not limited thereto.
The reaction between an aromatic diamine for obtaining a polyimide film, which can be preferably applied to the present invention, and an aromatic tetracarboxylic acid is carried out by reacting an aromatic diamine and an aromatic tetracarboxylic acid (anhydride) in a solvent. (Ring-opening) Polyamide acid solution that is a polyimide precursor is obtained by polyaddition reaction, and then a precursor film (green film) is formed from this polyamic acid solution, followed by drying, heat treatment, dehydration condensation (imide) Manufactured).

Although the polyimide film in this invention is not specifically limited, The combination of the following aromatic diamine and aromatic tetracarboxylic acid (anhydride) is mentioned as a preferable example.
A. A combination of an aromatic diamine having a benzoxazole structure and an aromatic tetracarboxylic acid.
B. A combination of an aromatic diamine having a diaminodiphenyl ether skeleton and an aromatic tetracarboxylic acid having a pyromellitic acid skeleton.
C. A combination of an aromatic diamine having a phenylenediamine skeleton and an aromatic tetracarboxylic acid having a biphenyltetracarboxylic acid skeleton.
D. A combination of one or more of the above ABCs.
Examples of aromatic diamines having a benzoxazole structure that can be preferably used in the present invention include the following compounds.

  2,2′-p-phenylenebis (5-aminobenzoxazole), 2,2′-p-phenylenebis (6-aminobenzoxazole), 1- (5-aminobenzoxazolo) -4- (6- Aminobenzoxazolo) benzene, 2,6- (4,4′-diaminodiphenyl) 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 '] bis-oxazole.

Among these, amino (aminophenyl) benzoxazole isomers are preferable from the viewpoint of easy synthesis. Here, “each isomer” refers to each isomer in which two amino groups of amino (aminophenyl) benzoxazole are determined according to the coordination position (eg, the above “formula 1” to “formula 4”). Each compound described in the above. These diamines may be used alone or in combination of two or more.
In the present invention, it is preferable to use 70 mol% or more of the aromatic diamine having the benzoxazole structure.

Examples of the aromatic diamine having a diaminodiphenyl ether skeleton in the present invention include 4,4′-diaminodiphenyl ether (DADE), 3,3′-diaminodiphenyl ether, 3,4′-diaminodiphenyl ether, and derivatives thereof.
Examples of the aromatic diamine having a phenylenediamine skeleton in the present invention include p-phenylenediamine, m-phenylenediamine, o-phenylenediamine and derivatives thereof.

You may use the following aromatic diamine which is not limited to the above for the polyimide film in this invention.
For example, 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-aminobenzylamine, p-aminobenzylamine,

  3,3′-diaminodiphenyl sulfide, 3,3′-diaminodiphenyl sulfoxide, 3,4′-diaminodiphenyl sulfoxide, 4,4′-diaminodiphenyl sulfoxide, 3,3′-diaminodiphenyl sulfone, 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, -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-aminophenoxy) 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-dimethylphen Le] 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-aminophenoxy) 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-trifluoromethylphenoxy) -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-biphenoxy Nzophenone, 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 and the above fragrance Part or all of the hydrogen atoms on the aromatic ring in the aromatic diamine are halogen atoms, part or all of the hydrogen atoms of the alkyl group or alkoxyl group having 1 to 3 carbon atoms, the cyano group, or the alkyl group or alkoxyl group. And aromatic diamines substituted with a C 1-3 halogenated alkyl group or alkoxyl group substituted with.
As aromatic tetracarboxylic acids that can be preferably used in the polyimide film of the present invention, aromatic tetracarboxylic acids having a pyromellitic acid skeleton, that is, pyromellitic acid and anhydrides or halides thereof, and aromatic tetracarboxylic acids having a biphenyltetracarboxylic acid skeleton are used. Carboxylic acids, i.e. biphenyltetracarboxylic acid and anhydrides or halides thereof.
Without being limited thereto, the following aromatic tetracarboxylic acids may be used.

These tetracarboxylic acids may be used alone or in combination of two or more.

  The solvent used when polyamic acid is obtained by polymerizing aromatic diamines and aromatic tetracarboxylic acid anhydrides is particularly limited as long as it dissolves both the raw material monomer and the polyamic acid to be produced. Although not preferred, polar organic solvents are preferred, such as N-methyl-2-pyrrolidone, N-acetyl-2-pyrrolidone, N, N-dimethylformamide, N, N-diethylformamide, N, N-dimethylacetamide, dimethyl sulfoxide Hexamethylphosphoric amide, ethyl cellosolve acetate, diethylene glycol dimethyl ether, sulfolane, halogenated phenols and the like, among which N-methyl-2-pyrrolidone and N, N-dimethylacetamide are preferably applied. These solvents can be used alone or in combination. The amount of the solvent used may be an amount sufficient to dissolve the monomer as a raw material. As a specific amount used, the mass of the monomer in the solution in which the monomer is dissolved is usually 5 to 40% by mass, The amount is preferably 10 to 20% by mass.

Conventionally known conditions may be applied for the polymerization reaction for obtaining the polyamic acid (hereinafter also simply referred to as “polymerization reaction”). As a specific example, in a temperature range of 0 to 80 ° C., 10 Stirring and / or mixing continuously for 30 minutes. If necessary, the polymerization reaction may be divided or the temperature may be increased or decreased. In this case, the order of adding both monomers is not particularly limited, but it is preferable to add aromatic tetracarboxylic acid anhydrides to the solution of aromatic diamines. The mass of the polyamic acid in the polyamic acid solution obtained by the polymerization reaction is preferably 5 to 40% by mass, more preferably 10 to 30% by mass, and the viscosity of the solution is measured with a Brookfield viscometer (25 ° C.). From the viewpoint of the stability of liquid feeding, it is preferably 10 to 2000 Pa · s, and more preferably 100 to 1000 Pa · s.
The reduced viscosity (ηsp / C) of the polyamic acid in the present invention is not particularly limited, but is preferably 3.0 dl / g or more, more preferably 4.0 dl / g or more, and still more preferably 5.0 dl / g or more. preferable.

Moreover, you may perform superposition | polymerization by adding a small amount of terminal blockers to aromatic diamines before a polymerization reaction. Examples of the end capping agent include compounds having a carbon-carbon double bond such as maleic anhydride. The amount of maleic anhydride used is preferably 0.001 to 1.0 mole per mole of aromatic diamine.
Vacuum degassing during the polymerization reaction is effective in producing a good quality polyamic acid solution.
Further, in order to obtain the polyimide film of the present invention, it is possible to remove bubbles and dissolved gas in the solution in advance by treatment such as decompression when casting and applying a polyamic acid solution described below onto the support. This is an effective process.

  The support on which the polyamic acid solution is applied should have a smoothness and rigidity sufficient to form the polyamic acid solution into a film, and a drum or belt whose surface is made of metal, plastic, glass, porcelain, etc. And the like. A method using a polymer film having moderate rigidity and high smoothness is also a preferred embodiment. Among them, the surface of the support is preferably a metal, more preferably stainless steel that does not rust and has excellent corrosion resistance. The surface of the support may be plated with metal such as Cr, Ni, or Sn. The surface of the support can be mirror-finished or processed into a satin finish as required. The air volume and temperature in drying may be appropriately selected and adopted depending on the difference in the support, and the polyamic acid solution can be applied to the support by casting from a nozzle with a slit, extrusion by an extruder, squeegee coating, reverse coating, die Including, but not limited to, coating, applicator coating, wire bar coating and the like, conventionally known solution application means can be used as appropriate.

As imidization / heat treatment, a polyamic acid solution that does not contain a ring-closure (imidization) catalyst or a dehydrating agent is used, and the imidization reaction is advanced by subjecting to a heat treatment (so-called thermal ring closure method) or ring closure in the polyamic acid solution. Examples thereof include a chemical ring closure method in which a catalyst and a dehydrating agent are contained and an imidization reaction is performed by the action of the above ring closing catalyst and the dehydrating agent.
The heat treatment temperature of the thermal ring closure method is preferably 150 to 500 ° C. If the heat treatment temperature is lower than this range, it is difficult to sufficiently close the ring, and if it is higher than this range, the deterioration proceeds and the film tends to become brittle. A more preferable embodiment includes a two-stage heat treatment step having an initial stage heat treatment and a subsequent stage heat treatment in which a heat treatment is performed at 150 to 250 ° C. for 3 to 20 minutes and then heat treatment at 350 to 500 ° C. for 3 to 20 minutes.

The timing for adding the ring-closing catalyst to the polyamic acid solution is not particularly limited, and may be added in advance before the polymerization reaction for obtaining the polyamic acid. Specific examples of the ring-closing catalyst include aliphatic tertiary amines such as trimethylamine and triethylamine, and heterocyclic tertiary amines such as isoquinoline, pyridine, and betapicoline. Among them, heterocyclic tertiary amines are mentioned. At least one amine selected from is preferred. Although the usage-amount of a ring-closing catalyst with respect to 1 mol of polyamic acids does not have limitation in particular, Preferably it is 0.5-8 mol.
The timing of adding the dehydrating agent to the polyamic acid solution is not particularly limited, and may be added in advance before the polymerization reaction for obtaining the polyamic acid. Specific examples of the dehydrating agent include aliphatic carboxylic acid anhydrides such as acetic anhydride, propionic anhydride, butyric anhydride, and aromatic carboxylic acid anhydrides such as benzoic anhydride. Among them, acetic anhydride, benzoic anhydride, etc. Acids or mixtures thereof are preferred. Moreover, the usage-amount of the dehydrating agent with respect to 1 mol of polyamic acids is not particularly limited, but is preferably 0.1 to 4 mol. When a dehydrating agent is used, a gelation retarder such as acetylacetone may be used in combination.

Whether it is a thermal cyclization reaction or a chemical cyclization method, the polyimide film precursor (green sheet, film) formed on the support may be peeled off from the support before it is completely imidized. The film may be peeled after imidization.
Although the thickness of a polyimide film is not specifically limited, Considering using it for the base substrate for printed wiring boards mentioned later, it is 5-150 micrometers, Preferably it is 10-100 micrometers. This thickness can be easily controlled by the amount of the polyamic acid solution applied to the support and the concentration of the polyamic acid solution.
The polyimide film of the present invention is preferably provided with a lubricant in the polyimide to give fine irregularities on the film surface to improve the slipping property of the film.
As the lubricant, inorganic or organic fine particles having an average particle diameter of about 0.03 μm to 3 μm can be used. Specific examples include titanium oxide, alumina, silica, calcium carbonate, calcium phosphate, calcium hydrogen phosphate, calcium pyrophosphate, Examples include magnesium oxide, calcium oxide, and clay minerals.

When the polymer film of the present invention or a film made of a precursor thereof is subjected to a heat treatment or the like with a film end fixed tenter, the film end gripping at both ends in the width direction of the film is a large number of pins. A tenter type processing unit that consists of a sheet and a large number of pins arranged on each pin sheet, and that conveys the film while the pins are pierced at both ends of the film and stretched in the width direction and / or the conveying direction. The apparatus for producing a polymer film, comprising: means for cooling the pin so that the temperature of the pin is less than 180 ° C. when the pin pierces and conveys both side ends of the film. Will be described in detail.
A tenter using such a pin as a fixing means is called a pin tenter. The pin seat of the pin tenter is often combined with the drive chain and installed as an endless track. As for the drive chain of the pin tenter, a type that passes through the inside of the processing furnace is known for both reciprocations, and a type that the bag is arranged so as to pass outside the processing path. Preferably applied. In the case of such a type, the entire apparatus can be made compact.
As shown in FIG. 2, in the processing chamber that receives heat treatment or the like, a large number of pin sheets with a large number of pins are arranged at both ends of the film, and the individual pin sheets are arranged in series in the conveying direction on the innermost side. A plurality of pins and a plurality of other pins are provided, these pins grip and convey both ends of the film, and the plurality of pin sheets run parallel to each other at both ends of the film in the processing chamber, and The film is heat-treated while being kept at a very high temperature. At least in this chamber, both the pins and the pin sheet are exposed to a high temperature, the film heat-treatment is completed, the film is turned, and a new film is held again at the original position. It is like.
In the present invention, the cooling of the pins and the pin sheet is preferably performed between the return path of the drive chain on the entrance side of the processing path and the pinning zone.

In the conventional tenter type conveying apparatus, when the pins and the pin sheet grip the both ends of the film and start conveying, the film is heated by one end heat treatment temperature, for example, 450 ° C. and maintained at a high temperature without cooling means. In the piercing of both ends, it is difficult to maintain the uniformity of film gripping, and it becomes easier for the hole to expand or break in the width direction or the conveying direction of the film at the hole where the pin is engulfed. Therefore, in the present invention, the pin is provided with a cooling means immediately before returning to the position where the film heat treatment is finished and the film is turned and the film is gripped. The film is sufficiently cooled at the beginning, and the film grip uniformity is maintained at the piercing of both ends of the film with pins. It is prevented from that or fracture in the width direction or the conveying direction even pores of the film in the hole that has bite the emissions to expand occurs, a decrease in strain throughout the film, a reduction in film thickness unevenness can be achieved.
As a cooling means in the present invention, either air cooling or water cooling may be used, and a refrigerant other than air or water may be used. From the viewpoint of cooling efficiency, it is preferable to use a liquid refrigerant. Further, considering that the tenter itself is heated above the ignition point of a general organic solvent, it is most preferable to use a cooling means based on water cooling specifications. In order to prevent dew condensation in the vicinity of the cooling part, it is preferable to control the dew point of the cold air when air is used as the atmosphere and the refrigerant.

EXAMPLES Hereinafter, although an Example and a comparative example are shown and this invention is demonstrated more concretely, this invention is not limited by a following example. In addition, the evaluation method of the physical property in the following examples is as follows.
1. Reduced viscosity of polyamic acid (ηsp / C)
A solution dissolved in N-methyl-2-pyrrolidone (or N, N-dimethylacetamide) so that the polymer concentration was 0.2 g / dl was measured at 30 ° C. with an Ubbelohde type viscosity tube. (When the solvent used for preparing the polyamic acid solution was N, N-dimethylacetamide, the polymer was dissolved using N, N-dimethylacetamide and measured.)

2. Film thickness Measured using a micrometer (Millitron (registered trademark) 1245D, manufactured by Finelfu).
3. Tensile modulus, tensile breaking strength and tensile breaking elongation of the film Cut out a polyimide film to be measured into a strip of 100 mm × 10 mm in the flow direction (MD direction) and the width direction (TD direction), respectively, as a test piece did. Using a tensile tester (manufactured by Shimadzu Corp., Autograph (registered trademark), model name AG-5000A) under the conditions of a tensile speed of 50 mm / min and a distance between chucks of 40 mm, the tensile modulus, Tensile rupture strength and tensile rupture elongation were measured.

4). Film linear expansion coefficient (CTE)
The expansion / contraction rate was measured under the following conditions, and the range from 30 to 300 ° C. was divided at 15 ° C. intervals and obtained from the average value of the expansion / contraction rate / temperature of each divided range.
Device name: TMA4000S manufactured by MAC Science
Sample length; 20mm
Sample width: 2 mm
Temperature rise start temperature: 25 ° C
Temperature rising end temperature: 400 ° C
Temperature increase rate: 5 ° C / min
Atmosphere: Argon

5. Film melting point, glass transition temperature A sample was subjected to DSC measurement under the following conditions, and a melting point (melting peak temperature Tpm) and a glass transition point (Tmg) were determined under the following measurement conditions in accordance with JIS K7121.
Device name: DSC3100S manufactured by MAC Science
Pan ： Aluminum pan (non-airtight)
Sample mass: 4mg
Temperature rising start temperature: 30 ° C
Temperature increase rate: 20 ° C / min
Atmosphere: Argon 6. Thermal Decomposition Temperature of Film The thermal decomposition temperature was defined as a 5% mass loss after TGA measurement (thermobalance measurement) of a fully dried sample under the following conditions.
Device name: TG-DTA2000S manufactured by MAC Science
Pan ： Aluminum pan (non-airtight)
Sample mass: 10 mg
Temperature rising start temperature: 30 ° C
Temperature increase rate: 20 ° C / min
Atmosphere: Argon

[Reference Example 1]
(Preliminary dispersion of inorganic particles)
1.22 parts by mass of amorphous silica spherical particles Seahoster KE-P10 (manufactured by Nippon Shokubai Co., Ltd.), 420 parts by mass of N-methyl-2-pyrrolidone, the wetted part of the container, and the infusion pipe are austenitic stainless steel The mixture was placed in a container of SUS316L and stirred with a homogenizer T-25 basic (manufactured by IKA Labortechnik) at a rotation speed of 1000 rpm for 1 minute to obtain a preliminary dispersion. The average particle size in the preliminary dispersion was 0.11 μm.
(Preparation of polyamic acid solution)
A nitrogen inlet tube, a thermometer, a liquid contact part of a container equipped with a stirring rod, and a pipe for infusion were substituted with nitrogen in the reaction container made of austenitic stainless steel SUS316L, and then 223 parts by mass of 5-amino-2- ( p-Aminophenyl) benzoxazole was added. Next, 4000 parts by mass of N-methyl-2-pyrrolidone was added and completely dissolved, and then the preliminary dispersion obtained above was added with 420 parts by mass and 217 parts by mass of pyromellitic dianhydride. When the mixture was stirred at ° C. for 24 hours, a brown viscous polyamic acid solution A was obtained. The reduced viscosity (ηsp / C) was 3.8 dl / g.

[Reference Example 2]
Nitrogen introduction tube, thermometer, vessel wetted part equipped with stirring rod, and infusion pipe were replaced with nitrogen in the reaction vessel of austenitic stainless steel SUS316L, and then 5-amino-2- (p-aminophenyl) ) Snowtex DMAC-ST30 (manufactured by Nissan Chemical Industries, Ltd.), in which 223 parts by mass of benzoxazole and 4416 parts by mass of N, N-dimethylacetamide were completely dissolved and then colloidal silica was dispersed in dimethylacetamide. When 40.5 parts by mass (including 8.1 parts by mass of silica) and 217 parts by mass of pyromellitic dianhydride are added and stirred at a reaction temperature of 25 ° C. for 24 hours, a brown and viscous polyamic acid solution B is obtained. It was. Ηsp / C of this product was 4.0 dl / g.

[Reference Example 3]
(Preliminary dispersion of inorganic particles)
7.6 parts by weight of amorphous silica spherical particle Seahoster KE-P10 (manufactured by Nippon Shokubai Co., Ltd.), 390 parts by weight of N-methyl-2-pyrrolidone, the liquid contact part of the container, and the infusion pipe are austenitic stainless steel SUS316L And stirred for 1 minute at a rotation speed of 1000 rpm with a homogenizer T-25 basic (manufactured by IKA Labortechnik) to obtain a preliminary dispersion.
(Preparation of polyamic acid solution)
The liquid contact part of the vessel equipped with a nitrogen introduction tube, a thermometer, a stirring rod, and the pipe for infusion were substituted with nitrogen in the reaction vessel made of austenitic stainless steel SUS316L, and then 200 parts by mass of diaminodiphenyl ether was added. Next, after 3800 parts by mass of N-methyl-2-pyrrolidone was added and completely dissolved, 390 parts by mass and 217 parts by mass of pyromellitic dianhydride were added to the preliminary dispersion obtained above. When the mixture was stirred at 0 ° C. for 5 hours, a brown viscous polyamic acid solution C was obtained. The reduced viscosity (ηsp / C) was 3.7 dl / g.

[Reference Example 4]
(Preliminary dispersion of inorganic particles)
3.7 parts by mass of amorphous silica spherical particles Seahoster KE-P10 (manufactured by Nippon Shokubai Co., Ltd.), 420 parts by mass of N-methyl-2-pyrrolidone, and the infusion part are austenitic stainless steel SUS316L And stirred for 1 minute at a rotation speed of 1000 rpm with a homogenizer T-25 basic (manufactured by IKA Labortechnik) to obtain a preliminary dispersion.
(Preparation of polyamic acid solution)
The wetted part of the vessel equipped with a nitrogen introduction tube, a thermometer, and a stirring rod, and the infusion piping were substituted with nitrogen in the reaction vessel made of austenitic stainless steel SUS316L, and then 108 parts by mass of phenylenediamine was added. Next, after 3600 parts by mass of N-methyl-2-pyrrolidone was added and completely dissolved, 420 parts by mass and 292.5 parts by mass of diphenyltetracarboxylic dianhydride were added to the preliminary dispersion obtained above. When the mixture was stirred at 25 ° C. for 12 hours, a brown viscous polyamic acid solution D was obtained. The reduced viscosity (ηsp / C) was 4.5 dl / g.

[Examples 1 to 4]
The polyamic acid solution obtained in Reference Examples 1 to 4 was coated on the non-lubricant surface of polyethylene terephthalate film A-4100 (manufactured by Toyobo Co., Ltd.) using a comma coater (gap: 150 μm, coating) And dried at 90 ° C. for 60 minutes. The polyamic acid film which became self-supporting after drying was peeled off from the support and cut at both ends to obtain respective green films having a thickness of 21 μm and a width of 1200 mm.
As shown in FIG. 1, the obtained green film has a pin sheet in which pins are arranged so that the pin interval is constant when the pin sheets are arranged, and a pin and The pin sheet is passed through a pin tenter having a cooling mechanism by water cooling of the pin sheet (FIG. 2), the pin sheet interval is 1140 mm, that is, each 30 mm at both ends of the green film is inserted into the pin, the first stage is 200 ° C. for 5 minutes, and the heating rate is 4 The temperature was raised at 0 ° C./second, and the second stage was heated at 450 ° C. for 5 minutes as a second stage to advance the imidization reaction. In addition, the temperature of the pin and pin sheet immediately before pin stab was controlled in a range of 150 ° C. plus or minus 8 ° C.
The conveyance state of the film was good, and the pin did not slip out in the tenter. The film tear width at the pin piercing portion at the tenter outlet was within about 1 mm.
The obtained film was cooled to room temperature, portions with poor flatness at both ends of the film were cut off with a slitter, rolled up into a roll, and each polyimide film of Examples 1 to 4 exhibiting brown color was obtained. The measurement results such as the properties of the obtained polyimide film are shown in Table 1. Here, the length of the pin sheet is 65.0 mm, and the pin interval is 7.0 mm.

The flatness and effective width of the film were defined as follows.
First, the obtained film was spread on a surface plate having a clean surface, and a portion where a space was left between the surface plate due to undulation at the end of the film was regarded as a portion having poor flatness. The ends of the film were not lifted from the surface of the platen, and both ends of the film were cut until the entire film was in close contact with the platen, and the film width at that time was defined as the effective width.

[Examples 5 to 12]
Hereinafter, film formation was carried out in the same manner as in the Examples while changing the temperature of the pin and the pin sheet, and evaluation was performed. The results are shown in Table 2.

[Comparative Examples 1-4]
The polyamic acid solutions of Reference Examples 1 to 4 were applied and dried on a support in the same manner as in Examples, and the polyamic acid film that became self-supporting after drying was peeled off from the support, and each green having a thickness of 21 μm. A film was obtained.
These obtained green films were heat-treated with a pin tenter in the same manner as in Example 1. In the comparative example, the pins and the pin sheet are not cooled. During film formation, the temperature of the pins and the pin sheet changed in the range of about 205 ° C plus or minus 12 ° C.
Hereafter, the part with bad flatness of the both ends of a film was cut off with the slitter similarly to the Example, it rolled up in roll shape, and each polyimide film of Comparative Examples 1-4 which exhibits brown was obtained. Results such as the properties of the obtained polyimide film are shown in Table 1.
As a result, it can be seen that in the comparative example, the pin is likely to be dislodged, the pin tear is large, the width of the portion having poor flatness at the film end is wide, and as a result, the effective width is narrow.

In the case of producing a polymer film, particularly a polyimide film, when the present invention is carried out by using a tenter type conveying device for drying and heat treatment, a long hole shape is formed in the width direction of the film at the hole in which the pin is bitten. A manufacturing apparatus having a pin and pin sheet cooling means suitable for manufacturing a polymer film that can suppress the problem of breakage of the film, and a method for manufacturing a polymer film using the apparatus, and a film gripping portion (pin The pin is sufficiently cooled at the start of film gripping at the piercing portion), and the breakage is reduced in the shape of a long hole outward in the width direction of the film at the hole where the pin is pierced. Reduction in thickness unevenness can be achieved, and high-quality polyimide films such as high-quality polyimide films with excellent film quality in the width direction and uniformity in film thickness can be easily obtained. Also contribute to the productivity of the polymer film production, it is industrially extremely significant as a production method for a polymer film as a production apparatus of the polymer film.
It is a manufacturing device and manufacturing method effective as a casting film forming method for polyimide film, cellulose film, polyamide film, polyamideimide film, etc., and is industrially significant.

The outline of the pin sheet in the tenter type film processing machine of the present invention is shown. The whole outline in the tenter type film processing machine of the present invention is shown.

Claims (2)

  When a film made of a polymer film or a precursor thereof is subjected to a heat treatment or the like with a film end fixed tenter, the film end gripping at both end portions in the width direction of the film is performed individually with a large number of pin sheets. A high-tensile processing unit that transports the film in a state where the film is stretched in the width direction and / or the transport direction. In the molecular film manufacturing apparatus, it has a means to cool so that the temperature of a pin may be less than 180 degreeC when this pin stabs and conveys both ends of a film, and it has a means to cool.   When a film made of a polymer film or a precursor thereof is subjected to a heat treatment or the like with a film end fixed tenter, the film end gripping at both end portions in the width direction of the film is performed individually with a large number of pin sheets. A high-tensile processing unit that transports the film in a state where the film is stretched in the width direction and / or the transport direction. When a polymer film is produced using a molecular film production apparatus, the pin is cooled so that the temperature of the pin becomes less than 180 ° C. when the pin is pierced and conveyed at both ends of the film. A method for producing a film.