JP2007253517A - Polymer film manufacturing apparatus and polymer film manufacturing method - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a manufacturing apparatus suitable for the manufacture of a polymer film capable of reducing the thickness irregularity of the film or the breaking risk of the film caused by holding the film by clips in a case that drying or heating treatment is performed using a tenter type feed device when the polymer film, especially a polyimide film is manufactured, and a polymer film manufacturing method using the manufacturing apparatus. <P>SOLUTION: The polymer film manufacturing apparatus having a clip tenter type treatment part has a means for cooling the clips so that the temperature of the clips becomes below 180°C at the grasping start point of time when the polymer film or a polymer precursor film is grasped at both side edge parts thereof by the clips to be fed. The polymer film manufacturing method using the polymer film manufacturing apparatus is also disclosed. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

  The present invention relates to a production apparatus and production method for a polymer film, and in particular, a tenter type used when a precursor film is subjected to high-temperature heat treatment to form a polymer film during 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 film transporting processing unit. Moreover, it is related with the manufacturing method of the polymer film which uses this apparatus.

When a polyimide film is manufactured, a self-supporting polyimide precursor film (hereinafter also referred to as a green film) is imidized at a high temperature. In this case, a semi-dried self-supporting polyimide precursor film is conveyed. However, the polyimide film and the polyimide precursor film containing these solvents 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 large 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, many use of a tenter type conveying device for producing a polyimide film is also known (see Patent Documents 2 to 4).
Japanese Examined Patent Publication No. 39-029211 JP 09-188863 A Japanese Patent Laid-Open No. 11-254521 JP 09-073315 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 casting method while transporting it in the drying step. By using the film conveying apparatus, it is possible to suppress shrinkage of the film 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.

  Although film shrinkage occurs not only in the width direction of the film but in all directions, a conveyance tension acts in the film conveyance direction, 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 film tenter type transport device when drying and heat-treating.

  Among the film tenter type conveying devices, the film tenter type conveying device that holds the film in a stretched state in the width direction by biting a large number of clips along both side edges of the film was arranged in parallel. The clip is arranged and supported by a pair of moving chains. Compared to the pin tenter, this film tenter type transport device can disperse the stress on the gripping part, and does not cause film breakage due to pin tearing, and dust generation when the film is removed from the pin. There are advantages such as not. However, when an undried film is gripped, it is difficult to grip the film, and the film is likely to break in the form of fusing from the gripping part. However, carbonization occurs during repeated use and the gripping part is burnt, and there are problems such as deterioration of film flatness due to inhomogeneous gripping force and film contamination due to falling off of carbides.

  The present invention, when producing a polymer film such as a polyimide film, when using a tenter type conveying device in drying or heat treatment, prevents breakage at the clip portion and is excellent in flatness and cleanness. It is an object of the present invention to provide a manufacturing apparatus suitable for manufacturing a polymer film and a method for manufacturing a polymer film manufactured using the apparatus.

As a result of intensive studies, the present inventors have determined that the tenter temperature (when the film is transported by gripping both end portions of the film with a tenter when drying or heat-treating a polymer film such as a polyimide film by a tenter-type transport device is performed. It was found that by controlling the clip temperature in particular, it was possible to prevent film breakage and improve the flatness and cleanliness of the film, and created a polymer film production apparatus suitable for polymer film production.
That is, this invention consists of the following structures.
1. When a polymer film or a polymer precursor film is subjected to a heat treatment or the like with a film end fixed tenter, film end gripping at both ends in the width direction of the film is performed by sandwiching a plurality of clips. In a polymer film manufacturing apparatus having a tenter type processing section that transports a film in a state stretched in the width direction and / or the transport direction, the clip is cooled so that the temperature of the grip section in contact with the film is less than 180 ° C. An apparatus for producing a polymer film, characterized by comprising means for:
2. When a polymer film or a polymer precursor film is subjected to a heat treatment or the like with a film end fixed tenter, film end gripping at both ends in the width direction of the film is performed by sandwiching a plurality of clips. In a polymer film manufacturing apparatus having a tenter type processing section that transports a film in a state stretched in the width direction and / or the transport direction, the clip is cooled so that the temperature of the grip section in contact with the film is less than 180 ° C. A method for producing a polymer film.
3. The method for producing a polymer film according to claim 2, wherein the polymer film is an aromatic polyamide film or a polyimide film.

The polymer film production apparatus of the present invention is a tenter type processing unit (conveying device) in a polymer film such as a polyimide film, while the clips on both sides of the film are running in parallel with the clips on the opposite side, Since the clip is cooled to less than 180 ° C. when gripping the film, deformation of the film is suppressed in the initial stage of gripping the film. More specifically, when an undried film is gripped by a clip whose temperature is not controlled, the solvent is rapidly volatilized from the film, and many voids are generated in the vicinity of the gripped portion. Therefore, the mechanical strength of the film becomes weak, and the film cannot withstand the stress caused by the wind pressure or its own weight in the tenter, resulting in breakage.
Such a phenomenon is not limited to the breaking of the film, but promotes a secondary phenomenon that a film component or a part of the decomposed product easily adheres to the clip holding portion. These organic components adhering to the clip carbonize during repeated use and contaminate the clip. In a contaminated clip, the film cannot be gripped uniformly, and the stress balance in the width direction is lost, causing stress inhomogeneity in the produced film, resulting in the plane of the resulting film In addition, the mechanical properties are lowered, and further, in-plane variations in mechanical properties are caused. Further, when such carbides fall off, they become black conductive foreign matters, which not only harm the appearance but also adversely affect the electrical reliability.
In the present invention, by controlling the temperature of the clip part, the generation of voids at the film gripping part and the adhesion of film components to the clip side are suppressed, so that such problems are eliminated and a high-quality and clean film is efficiently produced. It can be manufactured economically well, contributes to the productivity of polymer film production, and is industrially extremely effective as a polymer film production apparatus and a polymer film production 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 particularly 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 '] bisoxazole l.

Among these, amino (aminophenyl) benzoxazole isomers are preferable from the viewpoint of ease of 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.

これらのテトラカルボン酸は単独で用いてもよいし、二種以上を併用してもよい。

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 mol per mol of aromatic diamine.
Vacuum degassing during the polymerization reaction is effective in producing a good quality polyamic acid solution.
Furthermore, 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 is only required to have 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 film) formed on the support may be peeled off from the support before it is completely imidized. You may peel after conversion.
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.

In the present invention, an end fixing tenter for heat-treating a polymer film or a film made of a precursor thereof is formed by sandwiching the film end gripping with a number of clips. The tenter of the present invention is characterized by having means for cooling so that the temperature of the gripping portion where the clip comes into contact with the film is less than 180 ° C.
Hereinafter, the clip cooling means will be described in detail. A tenter using such a clip as a fixing means is called a clip tenter. Clip tenter clips are often combined with drive chains and installed as endless tracks. As for the drive chain of the clip tenter, a type that passes through the inside of the processing furnace is known for both reciprocation, and a type that the return path passes through the inside of the processing furnace is known. It is preferable to apply to. In the case of such a type, the entire apparatus can be made compact.
As shown in FIG. 3, in a processing chamber that receives a heat treatment or the like, a large number of clip blocks in which clips are arranged are arranged at both ends of the film, and these clips grip and convey both ends of the film. These clips run parallel to each other at both ends of the film, and are kept at a very high temperature for heat treatment of the film. At least in this processing chamber, the clips are also exposed to high temperature, and the film heat treatment is completed. It turns and grips the film again in its original position.
In the present invention, the cooling of the clip and the clip block is preferably performed between the return path of the drive chain on the inlet side of the processing furnace and the clipping zone.

In the conventional tenter type transfer device, when these clips grip the both ends of the film and start to transfer, one end is heated to a heat treatment temperature of 490 ° C., for example, 490 ° C., and there is no cooling means or temperature control means, and temperature variation is maintained at a high temperature. In the gripping of both ends of the film by the clip, the film gripping uniformity is difficult to be maintained, film thickness spots and cracks are likely to occur in the vicinity of the portion sandwiched between the clips, and the film breaks easily due to the expansion of the cracks. Furthermore, the distortion of the whole film increases and the film thickness unevenness increases. Therefore, in the present invention, a cooling means is provided at a position immediately before the clip is turned after the film heat treatment is finished and returns to the position where film gripping is started, and the clip is sufficiently cooled and temperature controlled at the time of starting film gripping. Therefore, uniformity of film gripping by the clip can be maintained, tearing in the vicinity of the clip, distortion reduction in the entire film, and 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.
Furthermore, in the present invention, it is preferable to include a means for measuring the temperature of the clip portion and a control system for controlling the degree of cooling according to the measurement result. As the temperature measuring means, a known means such as a thermocouple or a radiation thermometer can be used. The control system may use normal negative feedback control.

  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. The thickness of the polyimide film The thickness was measured using a micrometer (Millitron 1254D manufactured by Fine Reef).

3. Specimen obtained by cutting 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. It was. Using a tensile tester (manufactured by Shimadzu Corporation, Autograph (trade name), 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 of elasticity in each of the MD direction and TD direction, Tensile rupture strength and tensile rupture elongation were measured.

[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) ) After adding 223 parts by mass of benzoxazole and 4416 parts by mass of N, N-dimethylacetamide and completely dissolving them, Snowtex DMAC-ST30 (manufactured by Nissan Chemical Industries, Ltd.) 40 in which colloidal silica is dispersed in dimethylacetamide .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 to obtain a brown and viscous polyamide acid solution B. 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) using a comma coater (gap: 150 μm, coating width: 1240 mm). 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.
The obtained green films are shown in FIG. FIG. And a temperature measuring means of the clip gripping part by a radiation thermometer, and further FIG. Is passed through a clip tenter provided with a cooling section as shown in Fig. 1, the clip sheet interval is 1140 mm, that is, each 30 mm of both ends of the green film is held by clips, the first stage is 170 ° C for 5 minutes, the second stage Heating was performed at 220 ° C. for 5 minutes and the third stage at 480 ° C. for 5 minutes to advance the imidization reaction. The temperature at the clip gripping part was controlled in the range of 160 ° C. plus or minus 5 ° C.
The conveyance state of the film was good, and “clip disengagement” did not occur in the tenter. Also, almost no film tearing was observed even at the clip gripping portion at the tenter exit.
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. Table 1 shows the properties of the obtained polyimide film.

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 clip, 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 clip tenter in the same manner as in Example 1. In the comparative example, the clip is not cooled. During the film formation, the temperature of the clip changed in the range of about 220 ° C plus or minus 10 ° 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 shown in the results, it can be seen that in the comparative example, the clip is easily displaced, the clip tear is large, the width of the portion having poor flatness at the film end is wide, and the effective width is narrowed as a result.

In the present invention, when producing a polymer film, particularly a polyimide film or a polyamide film, when drying or heat treatment is carried out using a tenter type conveying device, the width direction of the film in the hole in which the clip is entrapped A manufacturing apparatus having a clip and clip sheet cooling means suitable for manufacturing a polymer film capable of suppressing the problem of breaking into a long hole, and a manufacturing method of the polymer film manufactured using the apparatus, and gripping the film At the start of gripping the film at the part (clip piercing part), the clip is sufficiently cooled, 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 clip is pierced, and the distortion of the entire film is reduced. Reduction of film thickness unevenness can be achieved, and the film is a high-quality polymer with excellent quality in the width direction and uniformity in film thickness. Easily polymeric films such as bromide film is obtained, also contributed 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 side surface outline of the clip part in the clip tenter of the present invention is shown.

The front outline of the clip part in the clip tenter of the present invention is shown.

The whole outline in the clip tenter of the present invention is shown.

Explanation of symbols

1. Clip movable part Roller 3. Clip gripping part 4. Rotating shaft 11. Cooling unit 12. Heat treatment zone 13. Clip drive chain

Claims (3)

  When a polymer film or a polymer precursor film is subjected to a heat treatment or the like with a film end fixed tenter, film end gripping at both ends in the width direction of the film is performed by sandwiching a plurality of clips. In a polymer film manufacturing apparatus having a tenter type processing section that transports a film stretched in the width direction and / or the transport direction, the clip is cooled so that the temperature of the gripping section in contact with the film is less than 180 ° C. An apparatus for producing a polymer film, characterized by comprising means for:   When a polymer film or a polymer precursor film is subjected to a heat treatment or the like with a film end fixed tenter, film end gripping at both ends in the width direction of the film is performed by sandwiching a plurality of clips. In a polymer film manufacturing apparatus having a tenter type processing section that transports a film stretched in the width direction and / or the transport direction, the clip is cooled so that the temperature of the gripping section in contact with the film is less than 180 ° C. A method for producing a polymer film.   The method for producing a polymer film according to claim 2, wherein the polymer film is an aromatic polyamide film or a polyimide film.

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