WO2016148150A1 - Novel tetracarboxylic dianhydride, and polyimide and polyimide copolymer obtained from said acid dianhydride - Google Patents
Novel tetracarboxylic dianhydride, and polyimide and polyimide copolymer obtained from said acid dianhydride Download PDFInfo
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- WO2016148150A1 WO2016148150A1 PCT/JP2016/058182 JP2016058182W WO2016148150A1 WO 2016148150 A1 WO2016148150 A1 WO 2016148150A1 JP 2016058182 W JP2016058182 W JP 2016058182W WO 2016148150 A1 WO2016148150 A1 WO 2016148150A1
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- 0 C*1C(CN(C(c(c2c3)ccc3C(Oc3cc(Oc4cc(OC(c(cc5C([N+]6C)=O)ccc5C6=O)=O)ccc4C45c6ccccc6-c6c4cccc6)c5cc3)=O)=O)C2=O)C1 Chemical compound C*1C(CN(C(c(c2c3)ccc3C(Oc3cc(Oc4cc(OC(c(cc5C([N+]6C)=O)ccc5C6=O)=O)ccc4C45c6ccccc6-c6c4cccc6)c5cc3)=O)=O)C2=O)C1 0.000 description 1
- TWJFGHKBYPIOEL-UHFFFAOYSA-N Cc(cc1)cc(C(F)(F)F)c1-c(c(C(F)(F)F)c1)ccc1N(C(c(c1c2)ccc2C(Oc2cc(Oc3cc(OC(c(cc4)cc(C(N5C)=O)c4C5=O)=O)ccc3C34c(cccc5)c5-c5c3cccc5)c4cc2)=O)=O)C1=O Chemical compound Cc(cc1)cc(C(F)(F)F)c1-c(c(C(F)(F)F)c1)ccc1N(C(c(c1c2)ccc2C(Oc2cc(Oc3cc(OC(c(cc4)cc(C(N5C)=O)c4C5=O)=O)ccc3C34c(cccc5)c5-c5c3cccc5)c4cc2)=O)=O)C1=O TWJFGHKBYPIOEL-UHFFFAOYSA-N 0.000 description 1
- CXISKMDTEFIGTG-UHFFFAOYSA-N O=C(c(cc1)cc(C(O2)=O)c1C2=O)Oc(cc1)ccc1OC(c(cc1)cc(C(O2)=O)c1C2=O)=O Chemical compound O=C(c(cc1)cc(C(O2)=O)c1C2=O)Oc(cc1)ccc1OC(c(cc1)cc(C(O2)=O)c1C2=O)=O CXISKMDTEFIGTG-UHFFFAOYSA-N 0.000 description 1
- SMBTZHHGRSFIAZ-UHFFFAOYSA-N OC(c1c2ccc(C(Oc(cc3)cc(cc4)c3cc4OC(c(cc3)cc(C(O4)=O)c3C4=O)=O)=O)c1)OC2=O Chemical compound OC(c1c2ccc(C(Oc(cc3)cc(cc4)c3cc4OC(c(cc3)cc(C(O4)=O)c3C4=O)=O)=O)c1)OC2=O SMBTZHHGRSFIAZ-UHFFFAOYSA-N 0.000 description 1
- ZTQUBBFVYUHQRC-UHFFFAOYSA-N Oc1ccc(C2(c3ccccc3-c3c2cccc3)c(ccc(O)c2)c2O2)c2c1 Chemical compound Oc1ccc(C2(c3ccccc3-c3c2cccc3)c(ccc(O)c2)c2O2)c2c1 ZTQUBBFVYUHQRC-UHFFFAOYSA-N 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D407/00—Heterocyclic compounds containing two or more hetero rings, at least one ring having oxygen atoms as the only ring hetero atoms, not provided for by group C07D405/00
- C07D407/14—Heterocyclic compounds containing two or more hetero rings, at least one ring having oxygen atoms as the only ring hetero atoms, not provided for by group C07D405/00 containing three or more hetero rings
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G73/00—Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
- C08G73/06—Polycondensates having nitrogen-containing heterocyclic rings in the main chain of the macromolecule
- C08G73/10—Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
Definitions
- the present invention relates to a novel tetracarboxylic dianhydride having a spiro structure, and a polyimide and a polyimide copolymer obtained from the tetracarboxylic dianhydride.
- Non-patent Document 1 Polyimide that can withstand high temperatures of solder mounting temperature (260 ° C.) or more as a plastic material for microelectronics is widely used as an insulating layer for semiconductor elements and flexible printed wiring boards.
- solder mounting temperature 260 ° C.
- most of the polyimides with high heat resistance are poor in workability, and are mostly processed from a polyimide precursor, that is, a polyamic acid soluble in a solvent (Non-patent Document 1).
- a high temperature of 300 ° C. or higher is required, so the use may be limited depending on the imidization temperature.
- a polyimide film is produced from a polyamic acid film, depending on the thermal imidization conditions, there is a concern that film breakage due to curing shrinkage or voids are generated in the film, and imidation reaction control is very difficult.
- a high temperature furnace of 300 ° C. or higher is required at the time of imidization, and the production cost is increased.
- a polyimide that is soluble in a solvent (solvent-soluble polyimide) and a thermoplastic polyimide that can be melt-molded have been recently developed in the state where imidization has already been completed, and the processability is improved over conventional polyimides.
- Most of such polyimides have a polymer main chain such as a siloxane chain or an ether bond bent in the polyimide main chain to introduce a bond that easily undergoes intramolecular rotation, or a bulky substituent on the side chain.
- Non-patent Documents 2 and 3 To improve the workability by inhibiting the aggregation of polymer chains or reducing the concentration of imide groups in the main chain.
- such molecular design almost reduces the inherent heat resistance of polyimide with almost no exception. Accordingly, few polyimides have both heat resistance of 260 ° C. or higher, particularly 290 ° C. or higher, and high solvent solubility.
- Polyimides obtained from aromatic tetracarboxylic dianhydrides (electron-accepting) and aromatic diamines (electron-donating) are used for dipole-dipole interactions between carbonyl groups of imide rings and charge transfer interactions between molecules.
- the action strengthens the cohesive force between the polymer chains and restricts the molecular motion, and the glass transition temperature is much higher than that of general-purpose resins.
- the charge transfer interaction also occurs in the molecule, and most of the polyimide film has a very low light transmittance in the visible region due to the charge transfer interaction between the molecule and the molecule (Non-patent Document 4).
- the linear thermal expansion coefficient (CTE) of the film may be as low as that of an inorganic material, and the heat resistant film exhibits excellent thermal dimensional stability against heat. It becomes a material (Non-Patent Document 5).
- a polyimide film is a polyimide precursor soluble in a solvent, that is, a polyamic acid solution (varnish) is cast and dried on a support to form a polyamic acid film, which is then subjected to a dehydration ring-closing reaction at a high temperature ( It is manufactured by thermal imidization (Non-patent Document 1).
- thermal imidization it proceeds with the elimination of water as a by-product and residual solvent in the film, so a strong shrinkage force is generated along the film surface direction, and the film is fixed to a support. If it is, it will be apparently stretched.
- Non-Patent Documents 6 and 7 the polyimide chain is highly oriented along the film surface by such a stretching action. Due to this action, the polyimide film exhibits low thermal expansion, that is, excellent thermal dimensional stability.
- high dimensional stability polyimide is widely used as an insulating layer for semiconductor elements and flexible printed wiring boards.
- polyimides with excellent heat resistance and thermal dimensional stability are usually insoluble and infusible, so they have poor workability, and are processed into a film at the stage of a solvent-soluble precursor (polyamic acid). A process for thermal imidization of this must be selected. Since a high temperature of 300 ° C.
- Non-patent Document 7 a solution / thermoprocessable polyimide is required.
- a solution / thermoprocessable polyimide is to be obtained by a known method, there is almost no exception and the inherent heat resistance of the polyimide film is reduced and linear heat is applied. This leads to a significant increase in expansion coefficient (deterioration of thermal dimensional stability) (Non-patent Document 7).
- the present invention provides a tetracarboxylic dianhydride for providing a resin having both excellent solvent solubility (solution processability) and high heat resistance, and excellent solution processability synthesized from the tetracarboxylic dianhydride.
- An object is to provide a polyimide, a solution containing the polyimide, and a film having high heat resistance obtained from the polyimide and the polyimide solution.
- the present invention also provides a polyimide film obtained by applying and drying a polyimide copolymer and a solution containing the polyimide copolymer, and simultaneously having high heat resistance, low linear thermal expansion coefficient and high transparency. With the goal.
- the present inventors have obtained a polyimide having excellent solution processability from a tetracarboxylic dianhydride represented by the following formula (1), and a solution containing the polyimide From the above, it was found that a polyimide film having a heat resistance of 260 ° C. or higher was obtained, and the present invention was completed.
- the present invention is as follows.
- the present inventors also have a copolymer having a specific structure among polyimides containing a structure derived from the tetracarboxylic dianhydride represented by the above formula (1), that is, represented by the following formula (5).
- the polyimide copolymer having the repeating unit and the repeating unit represented by the following general formula (6) gives a stable polyimide solution at room temperature, and is coated and dried, so that it has high heat resistance and low linear heat.
- the inventors have found that a polyimide film having an expansion coefficient and high transparency can be obtained at the same time, and completed the present invention.
- the present invention is as follows.
- Y represents at least one tetravalent aromatic group selected from the group consisting of the following formulas (7) to (12)
- a polyimide having both high heat resistance (high glass transition temperature) and solvent solubility which has been extremely difficult to achieve with the prior art, a polyimide film produced from a solution containing the polyimide, and the polyimide are provided. It is possible to provide a tetracarboxylic dianhydride having a fluorene skeleton and a spiro skeleton.
- Example 4 is a chart of FT-IR measured in Example 2.
- 6 is a chart of FT-IR measured in Example 3.
- 6 is a chart of FT-IR measured in Example 4.
- 6 is a chart of FT-IR measured in Example 5.
- 6 is a chart of FT-IR measured in Example 6.
- 10 is a chart of FT-IR measured in Example 8.
- 10 is a chart of FT-IR measured in Example 10.
- 14 is a chart of FT-IR measured in Example 12.
- 18 is a chart of FT-IR measured in Example 14.
- 18 is a chart of FT-IR measured in Example 15.
- the tetracarboxylic dianhydride of the present invention has a structure represented by the following formula (1).
- the method for synthesizing the tetracarboxylic dianhydride represented by the formula (1) of the present invention is not particularly limited.
- a diol represented by the following formula (3) that is, spiro [fluorene-9,9′- (2 ′, 7′-dihydroxyxanthene)] or a diacetate thereof and trimellitic acid represented by the following formula (4) or a derivative thereof by a known esterification reaction.
- trimellitic acid derivatives include trimellitic anhydride and trimellitic anhydride halide.
- the structural characteristics of the tetracarboxylic dianhydride represented by the formula (1) according to the present invention include a spiro structure in which the xanthene structure and the fluorene structure are orthogonal to each other, and the phthalic anhydride moiety is converted to the xanthene structure via an ester bond. It is at the point where it joins.
- the polyimide represented by the following formula (2) uses the tetracarboxylic dianhydride represented by the above formula (1) as a raw material to obtain a useful polyimide having the above-mentioned specific physical properties. be able to.
- the production method is not particularly limited.
- the tetracarboxylic dianhydride represented by the above formula (1) is reacted with an aromatic or aliphatic compound having a divalent nucleophilic reactive functional group.
- a tetracarboxylic acid represented by the above formula (1) in a two-step synthesis method through a process of imidization or in a high boiling point solvent
- a one-step synthesis method in which an dianhydride and an aromatic or aliphatic compound having a divalent nucleophilic reactive functional group are reacted at 150 to 220 ° C. with stirring.
- the polyimide of the present invention has a structure represented by the following formula (2).
- X represents a divalent aromatic or aliphatic group.
- a divalent aromatic or aliphatic group represented by X is reacted with a tetracarboxylic dianhydride represented by the above formula (1) described later.
- an amino group, an isocyanate group, etc. are illustrated as a bivalent nucleophilic reactive functional group in this invention.
- aromatic or aliphatic compounds having a divalent nucleophilic reactive functional group include, for example, p-phenylenediamine, m-phenylenediamine, 4,4′-bis (4-aminophenoxy) biphenyl as diamines.
- the diisocyanates include 1,5-phenylene diisocyanate, 1,3-diisocyanatobenzene, 3,3′-dichloro-4,4′-diisocyanatobiphenyl, and 4,4′-diisocyanate.
- Aromatic diisocyanates such as dicyclomethane, alicyclic diisocyanates such as dicyclohexylmethane 4,4′-diisocyanate, and chain aliphatic diisocyanates such as hexamethylene diisocyanate. Two or more of these may be used in combination.
- An anhydride can be used in combination as a copolymerization component.
- aromatic tetracarboxylic dianhydrides that can be used in this case include pyromellitic dianhydride, 3,4,3 ′, 4′-biphenyltetracarboxylic dianhydride, 2,3,3 ′, 4.
- the aliphatic tetracarboxylic dianhydride is not particularly limited.
- the alicyclic one bicyclo [2.2.2] oct-7-ene-2,3,5,6-tetracarboxylic Acid dianhydride, 5- (dioxotetrahydrofuryl-3-methyl-3-cyclohexene-1,2-dicarboxylic acid anhydride, 4- (2,5-dioxotetrahydrofuran-3-yl) tetralin-1,2 -Dicarboxylic anhydride, tetrahydrofuran-2,3,4,5-tetracarboxylic dianhydride, bicyclo-3,3 ', 4,4'-tetracarboxylic dianhydride, 1,2,3,4 Examples thereof include cyclobutanetetracarboxylic dianhydride, 1,2,3,4-cyclopentanetetracarboxylic dianhydride, etc. Two or more of these may be used
- aprotic solvents such as N, N-dimethylformamide, N, N-dimethylacetamide, N-methyl-2-pyrrolidone, dimethyl sulfoxide and the like are preferable.
- any solvent can be used without any problem as long as the raw material, the polyimide precursor to be produced, and the imidized polyimide are dissolved and do not react with the raw material or the product. It is not limited to.
- amide solvents such as N, N-dimethylformamide, N, N-dimethylacetamide, N-methyl-2-pyrrolidone, ⁇ -butyrolactone, ⁇ -valerolactone, ⁇ -valerolactone, ⁇ -caprolactone, ⁇ -Ester solvents such as caprolactone, ⁇ -methyl- ⁇ -butyrolactone, butyl acetate, ethyl acetate and isobutyl acetate, carbonate solvents such as ethylene carbonate and propylene carbonate, glycol solvents such as diethylene glycol dimethyl ether, triethylene glycol and triethylene glycol dimethyl ether Phenol solvents such as phenol, m-cresol, p-cresol, o-cresol, 3-chlorophenol, 4-chlorophenol, cyclopentanone, cyclohexanone, acetone, methyl Ketone solvents such as ethyl ketone, di
- the method for synthesizing the tetracarboxylic dianhydride represented by the formula (1) of the present invention is not particularly limited, and a known esterification reaction can be appropriately used. Specifically, for example, a solution in which trimellitic anhydride chloride is dissolved in a dehydrated aprotic solvent and a diol of formula (3) and a deoxidizing agent are dissolved in the same solvent, using a mechanical stirrer or the like, Add in the temperature range of ⁇ 78 ° C. to 0 ° C., preferably ⁇ 30 ° C. to ⁇ 5 ° C. and stir for 0.5 to 48 hours, preferably 1 to 24 hours.
- the reaction solution is heated to 0 to 100 ° C., preferably 10 to 50 ° C., and stirred for 0.5 to 48 hours, preferably 1 to 24 hours to complete the esterification.
- the product is isolated from the solution containing the product, washed as appropriate, and dried at 20 to 220 ° C., more preferably at 50 to 200 ° C. with a vacuum dryer or the like, and is represented by the formula (1) of the present invention.
- Tetracarboxylic dianhydride can be obtained.
- the purity of the tetracarboxylic dianhydride represented by the formula (1) of the present invention is low, it can be appropriately purified by a known method such as a sublimation method or a recrystallization method.
- the method for synthesizing the polyimide represented by the above formula (2) of the present invention and the solution containing the polyimide is not particularly limited, and a known imidization reaction can be appropriately used.
- the divalent nucleophilic reactive functional group is an isocyanate group
- an aromatic or aliphatic diisocyanate is dissolved in a solvent
- the tetraisocyanate represented by the formula (1) is equimolar with the diisocyanate group.
- the solution containing the polyimide represented by the above formula (2) is preferably obtained by stirring for 1 to 72 hours.
- the divalent nucleophilic reactive functional group is an amino group
- an aromatic or aliphatic diamine is dissolved in a high boiling point solvent
- the tetracarboxylic acid represented by the formula (1) is equimolar with the diamine.
- an azeotropic agent such as toluene is added, and an inert gas is introduced at 150 to 220 ° C., more preferably at 160 to 190 ° C.
- imidation can be achieved by removing the water produced during imidization out of the system together with the azeotropic agent.
- a solution containing the polyimide represented by (2) can be obtained.
- the inside of the reaction vessel can be reduced in pressure, and the solid content concentration can be increased by this step.
- the polyimide represented by the above formula (2) of the present invention and the solution containing the polyimide can also be synthesized using the following two-step method.
- the divalent nucleophilic reactive functional group is an amino group
- an aromatic or aliphatic diamine is dissolved in a solvent, and this solution is represented by the formula (1) equimolar with the diamine.
- Tetracarboxylic dianhydride powder is added gradually or in portions, and a temperature of 0 to 100 ° C., more preferably 5 to 50 ° C. for 0.5 to 168 hours, using a mechanical stirrer or the like, More preferably, the polyamic acid solution which is a polyimide precursor is obtained by stirring for 1 to 96 hours.
- the solid concentration is preferably the maximum concentration at which the solution becomes uniform and can be stirred in order to maximize the molecular weight of the polyamic acid. That is, the solid content concentration is 1 to 50% by weight, more preferably 5 to 40% by weight. With such a solid content concentration, the degree of polymerization of the produced polyamic acid is sufficiently high.
- the solid content concentration during the polymerization is It is preferable to manage within a suitable concentration range.
- the second stage a method for imidizing the polyimide precursor obtained above, that is, polyamic acid, will be described as the second stage.
- well-known methods such as the high temperature solution imidation method thermally dehydrated and closed and the chemical imidation method using a dehydrating agent, can be used suitably.
- a solvent that can be used in producing the above-described polyamic acid to the polyamic acid solution obtained by the above method synthesized in a high boiling point solvent In particular, the same solvent as that used in the preparation of the polyamic acid is added to obtain an appropriate solution viscosity that is easy to stir. Further, an azeotropic agent such as toluene is added, and 150 to 220 ° C., more preferably while introducing an inert gas. , By stirring at 160 to 190 ° C.
- a solution containing polyimide represented by the above formula (2) can be obtained by imidization and simply returning the temperature to room temperature.
- a solvent that can be used for producing the above-described polyamic acid to the polyamic acid solution obtained by the above-described method in particular, the same solvent as that used for producing the polyamic acid is used.
- the solution viscosity is set to an appropriate level that is easy to stir, and while stirring with a mechanical stirrer or the like, an organic acid anhydride and a dehydrating cyclization agent (chemical imidization agent) composed of a tertiary amine as a basic catalyst are dropped.
- the imidization can be completed chemically by stirring at -100 ° C, preferably 10-50 ° C, for 1-72 hours.
- an organic acid anhydride which can be used in that case, An acetic anhydride, propionic anhydride, etc. are mentioned. Acetic anhydride is preferably used because of easy handling and separation of the reagent.
- the basic catalyst pyridine, triethylamine, quinoline and the like can be used, but pyridine is preferably used because of easy handling and separation of the reagent, but is not limited thereto.
- the amount of the organic acid anhydride in the chemical imidizing agent is in the range of 1 to 20 times mol, more preferably 1 to 10 times mol of the theoretical dehydration amount of the polyamic acid.
- the amount of the basic catalyst is in the range of 0.1 to 2 moles, more preferably in the range of 0.1 to 1 moles, relative to the amount of the organic acid anhydride.
- polyimide In the reaction solution obtained by the chemical imidization method, by-products (hereinafter referred to as impurities) such as bases, unreacted chemical imidization agents, and organic acids are mixed.
- impurities such as bases, unreacted chemical imidization agents, and organic acids are mixed.
- Polyimide may be isolated and purified.
- a known method can be used for purification. For example, as the simplest method, after dripping in a large amount of poor solvent while stirring the imidized reaction solution to precipitate polyimide, the polyimide powder is recovered and repeatedly washed until impurities are removed, A method of obtaining polyimide powder by drying under reduced pressure can be applied. At this time, the solvent that can be used is not particularly limited as long as it can precipitate polyimide, efficiently remove impurities, and can be easily dried.
- the concentration (solid content concentration) of the polyimide solution when dripped in the poor solvent is 20% by weight or less, more preferably 10% by weight or less.
- the amount of the poor solvent used at this time can be appropriately adjusted by those skilled in the art depending on the type of solvent and polyimide in the polyimide solution.
- the polyimide powder deposited as described above is collected, and the residual solvent is removed by vacuum drying or hot air drying.
- the drying temperature and time are not limited as long as the polyimide does not change in quality, and it is preferable to dry at a temperature of 30 to 150 ° C. for 3 to 24 hours.
- the polyimide powder represented by the above formula (2) thus obtained needs to be dissolved in a solvent in order to obtain a polyimide solution.
- the solvent that can be used can be appropriately selected according to the intended use and processing conditions of the polyamic acid solution.
- amide solvents such as N, N-dimethylformamide, N, N-dimethylacetamide, N-methyl-2-pyrrolidone, ⁇ -butyrolactone, ⁇ -valerolactone, ⁇ -valerolactone, ⁇ -caprolactone, ⁇ -caprolactone, ⁇ -methyl- ⁇ -butyrolactone, ester solvents such as butyl acetate, ethyl acetate and isobutyl acetate, carbonate solvents such as ethylene carbonate and propylene carbonate, glycols such as diethylene glycol dimethyl ether, triethylene glycol and triethylene glycol dimethyl ether Solvent, phenol solvents such as phenol, m-cresol, p-
- a low solvent such as triethylene glycol dimethyl ether, ⁇ -butyrolactone, or cyclopentanone may be used. It is preferable to use a hygroscopic solvent.
- amide solvents such as N, N-dimethylformamide, N, N-dimethylacetamide, N-methyl-2-pyrrolidone and the like, which are hygroscopic solvents, can be combined with the above low hygroscopic solvent to suppress the precipitation of polyimide. You can also.
- the polyimide powder can be dissolved in air or in an inert gas at a temperature ranging from room temperature to the boiling point of the solvent over 1 to 48 hours to form a polyimide solution.
- the intrinsic viscosity of the polyimide represented by the formula (2) of the present invention is preferably 0.1 dL / g or more, more preferably 0.2 dL / g or more in consideration of the film toughness of the polyimide film. If the intrinsic viscosity is less than 0.1 dL / g, the toughness of the polyimide film cannot be ensured, and the film may be brittle.
- the molecular weight of the polyimide of the present invention is preferably 5000 or more, more preferably 10,000 or more in terms of weight average molecular weight from the viewpoints of moldability and handleability.
- the molecular weight of the polyimide can be based on the viscosity of the polyimide solution.
- the polyimide solid content concentration in the polyimide solution can be appropriately selected according to the use of the solution. For example, in the case of a film, it depends on the molecular weight of the polyimide, the production method, and the desired film thickness.
- the solid concentration is preferably 5% by weight or more, preferably 5% by weight to 40% by weight. If the solid content concentration is too low, it may be difficult to form a film having a sufficient film thickness. Conversely, if the solid content concentration is high, the solution viscosity may be too high and coating may be difficult.
- the solid content concentration of the polyimide in this invention represents the content of the solid content (mainly polyimide represented by the said Formula (2)) remaining after removing a solvent from a polyimide solution by a usual method.
- the polyimide solution containing the polyimide represented by the above formula (2) of the present invention may include a release agent, a filler, a silane coupling agent, a crosslinking agent, a terminal sealing agent, an antioxidant, Additives such as foaming agents and leveling agents can be added.
- a polyimide solution on a support such as a glass substrate using a doctor blade or the like and then drying to prepare a polyimide film.
- a metal foil such as copper foil using a known method, for example, a doctor blade, and then dried to obtain a polyimide / metal foil laminated film, which can withstand high temperature processes during solder mounting. It can also be used for copper-clad laminates for flexible printed wiring boards.
- the polyimide solution is applied to an insulating material for a semiconductor or a flexible wiring board, the insulating layer can be easily formed by coating directly on the device and drying the solvent.
- the polyimide film produced as described above usually has a glass transition temperature of 260 ° C. or higher, particularly 290 ° C. or higher, so that it is particularly suitably used as a heat resistant film.
- a glass transition temperature of 260 ° C. or higher particularly 290 ° C. or higher, so that it is particularly suitably used as a heat resistant film.
- the glass transition temperature of the insulating layer is 260 ° C. or higher, it can sufficiently withstand 260 ° C., which is a lead-free solder mounting temperature, and is therefore preferably used as an insulating material.
- the polyimide copolymer of the present invention (hereinafter sometimes referred to as the polyimide of the present invention) has a repeating unit represented by the following formula (5) and a repeating unit represented by the following general formula (6).
- Y represents at least one tetravalent aromatic group selected from the group consisting of the following formulas (7) to (12).
- the polyimide copolymer of the present invention includes at least one tetracarboxylic dianhydride selected from the group consisting of a tetracarboxylic dianhydride represented by the following formula (13) and the following formulas (14) to (19): And a diamine represented by the following formula (20).
- Examples of the method for producing the polyimide copolymer of the present invention include at least one tetracarboxylic dianhydride represented by the above formula (13) and at least one tetracarboxylic acid selected from the group consisting of the above formulas (14) to (19).
- At least one tetracarboxylic dianhydride selected from the group consisting of the tetracarboxylic dianhydride represented by the above formula (13) and the above formulas (14) to (19) and the above formula (20)
- the represented diamine is reacted with stirring at 150 to 220 ° C.
- diamines can be used in combination with the diamine represented by the above formula (20) as long as the properties of the polyimide according to the present invention are not significantly impaired.
- Usable diamines include, for example, p-phenylenediamine, m-phenylenediamine, 4,4′-bis (4-aminophenoxy) biphenyl, bis (4- (3-aminophenoxy) phenyl) sulfone, bis (4- ( 4-aminophenoxy) phenyl) sulfone, 2,2-bis (4- (4-aminophenoxy) phenyl) propane, 2,2-bis (4- (4-aminophenoxy) phenyl) hexafluoropropane, 2,2 -Bis (4-aminophenyl) hexafluoropropane, p-terphenylenediamine, benzidine, 3,3'-dihydroxybenzidine, 3,3'-dimethoxybenzidine, o-tolidine, m-
- tetracarboxylic dianhydrides examples include 2,3,3 ′, 4′-biphenyltetracarboxylic dianhydride, 2,3,2 ′, 3′-biphenyltetracarboxylic dianhydride, 1, 4,5,8-naphthalene tetracarboxylic dianhydride, 3,4,3 ′, 4′-benzophenone tetracarboxylic dianhydride, 2,3,3 ′, 4′-benzophenone tetracarboxylic dianhydride, 2,3,2 ′, 3′-benzophenone tetracarboxylic dianhydride, 3,4,3 ′, 4′-biphenyl ether tetracarboxylic dianhydride, 3,4,2 ′, 3′-biphenyl ether tetracarboxylic dianhydride, 3,4,2 ′, 3′-biphenyl ether tetra Carboxylic dianhydride
- the solvent for synthesizing the polyimide copolymer or polyamic acid according to the present invention the solvents described above with respect to the polyimide according to the present invention can be used.
- the method for producing the tetracarboxylic dianhydride represented by the above formulas (13) to (19) used in the present invention is not particularly limited.
- the above formula (13) having an ester group in its structure and the tetracarboxylic dianhydride represented by the above formulas (17) to (19) are produced by appropriately using a known esterification reaction. .
- a solution in which trimellitic anhydride chloride is dissolved in a dehydrated aprotic solvent, and a solution in which a diol of the following formulas (21) to (24) and a deoxidizer are dissolved in a dehydrated aprotic solvent are used. After each preparation, these solutions are used in a temperature range of ⁇ 78 ° C.
- reaction solution is heated to 0 to 100 ° C., preferably 10 to 50 ° C., and stirred for 0.5 to 24 hours, preferably 1 to 12 hours to complete esterification, and then formed from a solution containing the product.
- the product is isolated, washed as appropriate, and dried at 100 to 220 ° C., more preferably 120 to 200 ° C. with a vacuum dryer or the like, so that the formula (13) and the formula (17) used in the present invention are used.
- a tetracarboxylic dianhydride represented by (19) can be obtained.
- the purity of the tetracarboxylic dianhydride represented by the above formula (13) and the above formulas (17) to (19) of the present invention is low, it is appropriately purified by a known method such as a sublimation method or a recrystallization method. it can.
- the method for synthesizing the polyimide copolymer of the present invention and the solution containing the polyimide copolymer is not particularly limited, and a known imidization reaction can be appropriately used.
- a known imidization reaction can be appropriately used.
- at least one tetracarboxylic dianhydride selected from the group consisting of the tetracarboxylic dianhydride represented by the above formula (13) and the above formulas (14) to (19) is used.
- the mixing ratio is usually selected from the group consisting of the above formulas (14) to (19) with respect to 1 mol of tetracarboxylic dianhydride represented by the above formula (13).
- At least one tetracarboxylic dianhydride is usually used in an amount of 1 to 99 mol%, preferably 2 to 70 mol%.
- a diamine represented by the above formula (20) is dissolved in a high boiling point solvent, and a tetracarboxylic dianhydride represented by the above formula (13) and the group consisting of the above formulas (14) to (19) are dissolved in this solution.
- an azeotropic agent such as toluene is added. The mixture is stirred at 150 to 220 ° C., more preferably 160 to 190 ° C.
- the solvent used at this time is not particularly limited as long as the polyimide copolymer is not precipitated.
- the polyimide copolymer of the present invention and the solution containing the polyimide copolymer can also be synthesized using the following two-step synthesis method.
- a diamine represented by the above formula (20) is dissolved in a solvent, and a tetracarboxylic dianhydride represented by the above formula (13) and the above formulas (14) to ( 19)
- a tetracarboxylic dianhydride represented by the above formula (13) and the above formulas (14) to ( 19) After adding the powder gradually or divided so that the total amount of tetracarboxylic dianhydride of at least one tetracarboxylic dianhydride selected from the group consisting of 19) is equimolar with diamine, mechanical stirrer
- the polyamic acid as the polyimide precursor is obtained by stirring at a temperature in the range of 0 to 100 ° C., more preferably 5 to 50 ° C.
- the solid concentration is preferably the maximum concentration at which the solution becomes uniform and can be stirred in order to maximize the molecular weight of the polyamic acid. That is, the solid content concentration is 1 to 50% by weight, more preferably 5 to 40% by weight. With such a solid content concentration, the degree of polymerization of the produced polyamic acid is sufficiently high.
- the solid content concentration during the polymerization is It is preferable to manage within a suitable concentration range.
- the polyimide precursor obtained above that is, the method of imidizing the polyamic acid is as described above for the polyimide according to the present invention.
- the polyimide copolymer powder thus obtained needs to be dissolved in a solvent in order to obtain a polyimide solution containing the polyimide copolymer of the present invention.
- Usable solvents include those described above with respect to the polyimide according to the present invention. Two or more of these may be mixed and used.
- the solvent in the polyimide solution absorbs moisture in the air and the polyimide copolymer may be precipitated, as described above for the polyimide according to the present invention.
- the content of the repeating unit represented by the above formula (5) and the repeating unit represented by the above formula (6) in the polyimide copolymer of the present invention is usually 1 to 99 mol%, and maintains low linear thermal expansion. Therefore, the content is preferably 2 to 70 mol%.
- the intrinsic viscosity of the polyimide copolymer of the present invention is as described above for the polyimide according to the present invention.
- the intrinsic viscosity in this invention represents the value measured by the method mentioned later.
- the molecular weight of the polyimide copolymer of the present invention is as described above for the polyimide according to the present invention.
- the solid content concentration of the polyimide solution containing the polyimide copolymer of the present invention can be appropriately selected according to the use of the solution.
- the solid content concentration is preferably 5% by weight or more. If the solid content concentration is too low, it may be difficult to form a film having a sufficient film thickness. Conversely, if the solid content concentration is high, the solution viscosity may be too high and coating may be difficult.
- the solid content concentration of the polyimide copolymer in the present invention represents the content of the solid content (mainly polyimide represented by the above formula (6)) remaining after removing the solvent from the polyimide solution by a conventional method.
- the additives that can be added to the polyimide solution containing the polyimide copolymer of the present invention are as described above with respect to the polyimide according to the present invention.
- the form of producing the polyimide film of the present invention using the polyimide solution containing the polyimide copolymer of the present invention is as described above for the polyimide according to the present invention.
- the polyimide film of the present invention produced as described above usually has a glass transition temperature of 260 ° C. or higher, for example, insulation for semiconductors and flexible wiring boards that can sufficiently withstand the lead-free solder mounting temperature of 260 ° C. It is suitably used as a material.
- the polyimide film of the present invention produced using the polyimide solution containing the polyimide copolymer of the present invention is characterized by high light transmittance and low linear thermal expansion, that is, usually the light transmittance at a wavelength of 400 nm is 30% or more, Moreover, since the linear thermal expansion coefficient is 40 ppm / K or less, it is excellent in transparency and thermal dimensional stability, so that it can be suitably used for various optical applications and optical devices.
- the present invention can also be expressed as follows.
- a polyimide solution comprising the polyimide according to [2] or the polyimide copolymer according to [3] or [4] in a solid content concentration of 5% by weight or more.
- a polyimide film comprising the polyimide according to [2], or the polyimide copolymer according to [3] or [4].
- [8] [3] or [4] polyimide film having the following characteristics (A), (B) and (C): (A) The light transmittance at a wavelength of 400 nm is 30% or more; (B) the coefficient of linear thermal expansion is 40 ppm / K or less; (C) Glass transition temperature (Tg) is 260 ° C. or higher.
- ⁇ Differential scanning calorimetry (melting point)> The melting point of tetracarboxylic dianhydride was measured at a heating rate of 5 ° C./min in a nitrogen atmosphere using a differential scanning calorimeter DSC3100 (Netch Japan). The higher the melting point and the sharper the melting peak, the higher the purity.
- ⁇ Intrinsic viscosity> The reduced viscosity of a 0.5 wt% polyimide precursor solution or polyimide solution was measured at 30 ° C. using an Ostwald viscometer. This value was regarded as the intrinsic viscosity.
- chloroform CF
- acetone tetrahydrofuran
- DOX 1,4-dioxane
- ethyl acetate cyclopentanone (CPN), cyclohexanone (CHN), N, N-dimethylformamide (DMF), N , N-dimethylacetamide (DMAc), N-methyl-2-pyrrolidone (NMP), m-cresol, dimethyl sulfoxide (DMSO), ⁇ -butyrolactone (GBL), triethylene glycol dimethyl ether (Tri-GL) were used.
- the evaluation results are ++ when dissolved at room temperature, + when dissolved by heating and maintaining uniformity after being allowed to cool to room temperature, ⁇ when swollen / partially dissolved, and ⁇ Is displayed.
- ⁇ Linear thermal expansion coefficient CTE and glass transition temperature: Tg>
- the glass transition temperature of the polyimide film is 5 ° C / min with TMA4000 manufactured by Netch Japan Co., Ltd. (sample size width 5 mm, length 15 mm) and the load (static load) is film thickness ( ⁇ m) ⁇ 0.5 g.
- Temporarily raised to 150 ° C first temperature rise
- cooled to 20 ° C further raised at 5 ° C / min (second temperature rise)
- the linear thermal expansion coefficient was determined as an average value between 100 and 200 ° C.
- T400 ⁇ Transmissivity of polyimide membrane: T400 > Using a UV-visible spectrophotometer V-530 (manufactured by JASCO Corp.), the light transmittance (T%) of the polyimide film at a wavelength of 200 to 800 nm was measured. A light transmittance of 400 nm was obtained as an index of transparency, and the transparency was evaluated.
- solution B was gradually added dropwise to solution A with a syringe, and then stirred at room temperature for 12 hours. After completion of the reaction, the yellow precipitate was filtered off and washed with DMF and ion exchange water. Removal of pyridine hydrochloride was confirmed using an aqueous silver nitrate solution. The washed product was collected and vacuum dried at 180 ° C. for 12 hours. The obtained product was a yellow powder, the yield was 4.8465 g, and the yield was 38.5%.
- Trimellitic chloride 4.3185 (20 mmol) was placed in an eggplant flask, dissolved in 11 mL of dehydrated THF at room temperature, and sealed with a septum to prepare solution A (solute concentration 30 wt%). Further, 1.6019 g (10.0 mmol) of 2,6-dihydroxynaphthalene was dissolved in 4.2 mL of dehydrated THF at room temperature in a separate flask (solute concentration 30 wt%). Prepared. While cooling and stirring in an ice bath, solution B was gradually added dropwise to solution A with a syringe, and then stirred at room temperature for 12 hours. After completion of the reaction, the pale yellow precipitate was filtered off and washed with THF and ion exchange water.
- the obtained crude product was purified by recrystallization from ⁇ -butyrolactone (GBL).
- the obtained product was obtained from a Fourier transform infrared spectrophotometer FT / IR-4100 (manufactured by JASCO Corporation) at 1857 cm ⁇ 1 and 1780 cm ⁇ 1 with an acid anhydride group C ⁇ O stretching vibration and at 1732 cm ⁇ 1 with an ester.
- the group C O stretching vibration was confirmed.
- Solution B 4.85 mL (60.0 mmol) of pyridine was added thereto, followed by septum sealing to prepare Solution B. While cooling and stirring in an ice bath, solution B was gradually added dropwise to solution A with a syringe and stirred for 1 hour, and then stirred at room temperature for 12 hours. After completion of the reaction, the white precipitate was filtered off and washed with THF and water. Removal of pyridine hydrochloride was confirmed by adding a silver nitrate aqueous solution to the washing solution and no white precipitate was observed. The washed product was collected and dried in vacuum at 100 ° C. for 12 hours. The obtained product was a white powder, the yield was 2.8336 g, and the yield was 39.8%.
- the obtained product was obtained from Fourier transform infrared spectrophotometer FT / IR-4100 (manufactured by JASCO Corporation) at 1856 cm ⁇ 1 and 1781 cm ⁇ 1 at acid anhydride group C ⁇ O stretching vibration absorption band, 1738 cm ⁇ 1.
- the ester group C O stretching vibration absorption band was confirmed.
- Example 2 Polyamide acid polymerization; DABA system 0.6818 g (3 mmol) of 4,4′-diaminobenzanilide (DABA) was dissolved in 6.57 g of dehydrated N, N-dimethylacetamide (DMAc). To this, 2.1378 g (3 mmol) of tetracarboxylic dianhydride powder represented by the formula (1) synthesized in Example 1 was slowly added and stirred at a solid content concentration of 30.0% by weight. While appropriately diluted with DMAc, the mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor (solid content concentration: 15.0% by weight). The intrinsic viscosity of the obtained polyamic acid was 1.41 dL / g.
- DABA 4,4′-diaminobenzanilide
- Example 3> Polyamide acid polymerization; 4,4'-ODA system 0.6007 g (3 mmol) of 4,4′-oxydianiline (4,4′-ODA) was dissolved in 6.39 g of dehydrated N, N-dimethylacetamide (DMAc). To this, 2.1378 g (3 mmol) of tetracarboxylic dianhydride powder represented by the formula (1) synthesized in Example 1 was slowly added and stirred at a solid content concentration of 30.0% by weight. While appropriately diluting with DMAc, the mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor (solid content concentration 22.9% by weight). The intrinsic viscosity of the obtained polyamic acid was 0.96 dL / g.
- Example 4> Polyamide acid polymerization; TFMB system 0.9607 g (3 mmol) of 4,4′-diamino-2,2′-bis (trifluoromethyl) biphenyl (TFMB) was dissolved in 7.2 g of dehydrated N, N-dimethylacetamide (DMAc). To this, 2.1378 g (3 mmol) of tetracarboxylic dianhydride powder represented by the formula (1) synthesized in Example 1 was slowly added and stirred at a solid content concentration of 30.0% by weight. While appropriately diluted with DMAc, the mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor (solid content concentration 23.6% by weight). The obtained polyamic acid had an intrinsic viscosity of 0.94 dL / g.
- Example 7 The polyimide powder obtained in Example 6 was redissolved in DMAc at room temperature to prepare a 10% by weight solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was dried again under reduced pressure at 280 ° C. for 1 hour. Table 4 shows the film physical properties of the obtained film.
- Example 8> Polyamide acid polymerization 0.9607 g (3 mmol) of the diamine represented by the formula (20) was dissolved in 6.9 g of dehydrated DMAc.
- Example 9 The polyimide powder obtained in Example 8 was redissolved in DMAc at room temperature to prepare a 20% by weight solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was again dried under reduced pressure at 250 ° C. for 1 hour. Table 4 shows the film physical properties of the obtained film.
- Example 11 The polyimide powder obtained in Example 10 was redissolved in DMAc at room temperature to prepare a 20% by weight solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was again dried under reduced pressure at 250 ° C. for 1 hour. Table 4 shows the film physical properties of the obtained film.
- Example 13 The polyimide powder obtained in Example 12 was redissolved in DMAc at room temperature to prepare a 12% by weight solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was again dried under reduced pressure at 250 ° C. for 1 hour. Table 4 shows the film physical properties of the obtained film.
- the obtained polyamic acid had an intrinsic viscosity of 2.26 dL / g.
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Abstract
Description
本発明は、本発明は、スピロ構造を有する新規なテトラカルボン酸二無水物、並びに該テトラカルボン酸二無水物から得られるポリイミド及びポリイミド共重合体に関する。 The present invention relates to a novel tetracarboxylic dianhydride having a spiro structure, and a polyimide and a polyimide copolymer obtained from the tetracarboxylic dianhydride.
マイクロエレクトロニクス用のプラスチック材料として半田実装温度(260℃)以上の高温に耐えるポリイミドは、半導体素子やフレキシブルプリント配線基板など絶縁層として広く用いられている。しかしながら、耐熱性の高いポリイミドの多くは加工性に乏しく、ポリイミドの前駆体、即ち溶媒に可溶なポリアミド酸から加工する場合がほとんどである(非特許文献1)。 Polyimide that can withstand high temperatures of solder mounting temperature (260 ° C.) or more as a plastic material for microelectronics is widely used as an insulating layer for semiconductor elements and flexible printed wiring boards. However, most of the polyimides with high heat resistance are poor in workability, and are mostly processed from a polyimide precursor, that is, a polyamic acid soluble in a solvent (Non-patent Document 1).
ポリアミド酸からポリイミドを形成するためには、300℃以上の高温を必要とするため、そのイミド化温度により用途が限定される場合がある。また、ポリアミド酸フィルムからポリイミドフィルムを製造する場合、熱イミド化条件によっては、硬化収縮によるフィルム破断やフィルム中にボイドが発生する懸念もあり、イミド化反応制御が非常に難しい。更には、イミド化時に300℃以上の高温炉が必要となり製造コストも高くなるという欠点があった。 In order to form a polyimide from a polyamic acid, a high temperature of 300 ° C. or higher is required, so the use may be limited depending on the imidization temperature. Further, when a polyimide film is produced from a polyamic acid film, depending on the thermal imidization conditions, there is a concern that film breakage due to curing shrinkage or voids are generated in the film, and imidation reaction control is very difficult. Furthermore, there is a drawback that a high temperature furnace of 300 ° C. or higher is required at the time of imidization, and the production cost is increased.
そこで、既にイミド化が完結している状態で溶媒に可溶なポリイミド(溶媒可溶性ポリイミド)や、溶融成型可能な熱可塑性ポリイミドが近年開発され、従来のポリイミドよりも加工性が改善されている。このようなポリイミドの大部分は、ポリイミド主鎖中にシロキサン鎖やエーテル結合のような高分子主鎖を屈曲させ、分子内回転運動がし易い結合を導入したり、側鎖に嵩高い置換基を入れ高分子鎖の凝集を阻害したり、主鎖中のイミド基濃度を低下させるなどして加工性を高めている(非特許文献2,3)。しかしながら、このような分子設計は、ほぼ例外なくポリイミド本来の耐熱性を著しく低下させてしまう。従って、260℃以上、特に290℃以上の耐熱性と高い溶媒溶解性を兼ね備えたポリイミドは、ほとんど知られていない。 Therefore, a polyimide that is soluble in a solvent (solvent-soluble polyimide) and a thermoplastic polyimide that can be melt-molded have been recently developed in the state where imidization has already been completed, and the processability is improved over conventional polyimides. Most of such polyimides have a polymer main chain such as a siloxane chain or an ether bond bent in the polyimide main chain to introduce a bond that easily undergoes intramolecular rotation, or a bulky substituent on the side chain. To improve the workability by inhibiting the aggregation of polymer chains or reducing the concentration of imide groups in the main chain (Non-patent Documents 2 and 3). However, such molecular design almost reduces the inherent heat resistance of polyimide with almost no exception. Accordingly, few polyimides have both heat resistance of 260 ° C. or higher, particularly 290 ° C. or higher, and high solvent solubility.
また、芳香族テトラカルボン酸二無水物(電子受容性)と芳香族ジアミン(電子供与性)から得られるポリイミドは、イミド環のカルボニル基間双極子・双極子相互作用や分子間の電荷移動相互作用によって高分子鎖間の凝集力が強まり分子運動が制限され、ガラス転移温度が汎用樹脂に比べて遥かに高くなる。電荷移動相互作用は分子内でも生じ、分子内と分子間の電荷移動相互作用によってポリイミドフィルムの多くは、可視領域の光透過率が非常に低くなる(非特許文献4)。また、直線的で剛直な化学構造を有するポリイミドでは、フィルムの線熱膨張係数(CTE)が無機材料と同程度まで低くなる場合があり、熱に対して優れた熱寸法安定性を示す耐熱フィルム材料となる(非特許文献5)。 Polyimides obtained from aromatic tetracarboxylic dianhydrides (electron-accepting) and aromatic diamines (electron-donating) are used for dipole-dipole interactions between carbonyl groups of imide rings and charge transfer interactions between molecules. The action strengthens the cohesive force between the polymer chains and restricts the molecular motion, and the glass transition temperature is much higher than that of general-purpose resins. The charge transfer interaction also occurs in the molecule, and most of the polyimide film has a very low light transmittance in the visible region due to the charge transfer interaction between the molecule and the molecule (Non-patent Document 4). In addition, in a polyimide having a linear and rigid chemical structure, the linear thermal expansion coefficient (CTE) of the film may be as low as that of an inorganic material, and the heat resistant film exhibits excellent thermal dimensional stability against heat. It becomes a material (Non-Patent Document 5).
一般に、ポリイミドフィルムは、溶媒に可溶なポリイミドの前駆体、即ちポリアミド酸の溶液(ワニス)を支持体上に流延・乾燥してポリアミド酸フィルムとした後に、これを高温で脱水閉環反応(熱イミド化)させて製造される(非特許文献1)。一般に、熱イミド化の際、副生成物である水やフィルム中の残留溶媒の脱離を伴いながら進行するためフィルム面方向に沿って強い収縮力が発生し、フィルムが支持体等に固定されている場合は、見かけ上延伸されることになる。直線的で剛直な化学構造を有するポリイミド系では、このような延伸作用により、ポリイミド鎖はフィルム面に沿って高度に配向する(非特許文献6,7)。この作用により、前記ポリイミドフィルムは低熱膨張性、即ち優れた熱寸法安定性を示すようになる。現在、高寸法安定性ポリイミドは、半導体素子やフレキシブルプリント配線基板などの絶縁層として広く使用されている。しかしながら、耐熱性および熱寸法安定性に優れたポリイミドは通常、不溶・不融であるため加工性に乏しく、溶媒に可溶な前駆体(ポリアミド酸)の段階でフィルム状に加工しておき、これを熱イミド化する工程を選択せざるを得ない。熱イミド化工程では、300℃以上の高温を必要とするため、無着色透明なポリイミドフィルムが求められる用途(特に光学デバイス)では、このような高温製膜プロセスは不利である。そこで、上述したように、溶液・熱加工性ポリイミドが求められているが、公知の方法により溶液・熱加工性ポリイミドを得ようとすると、ほぼ例外なくポリイミドフィルム本来の耐熱性の低下および線熱膨張係数の著しい増大(熱寸法安定性の悪化)を招くことになる(非特許文献7)。 In general, a polyimide film is a polyimide precursor soluble in a solvent, that is, a polyamic acid solution (varnish) is cast and dried on a support to form a polyamic acid film, which is then subjected to a dehydration ring-closing reaction at a high temperature ( It is manufactured by thermal imidization (Non-patent Document 1). In general, during thermal imidization, it proceeds with the elimination of water as a by-product and residual solvent in the film, so a strong shrinkage force is generated along the film surface direction, and the film is fixed to a support. If it is, it will be apparently stretched. In a polyimide system having a linear and rigid chemical structure, the polyimide chain is highly oriented along the film surface by such a stretching action (Non-Patent Documents 6 and 7). Due to this action, the polyimide film exhibits low thermal expansion, that is, excellent thermal dimensional stability. Currently, high dimensional stability polyimide is widely used as an insulating layer for semiconductor elements and flexible printed wiring boards. However, polyimides with excellent heat resistance and thermal dimensional stability are usually insoluble and infusible, so they have poor workability, and are processed into a film at the stage of a solvent-soluble precursor (polyamic acid). A process for thermal imidization of this must be selected. Since a high temperature of 300 ° C. or higher is required in the thermal imidization step, such a high-temperature film forming process is disadvantageous in applications (particularly optical devices) where a non-colored transparent polyimide film is required. Therefore, as described above, a solution / thermoprocessable polyimide is required. However, if a solution / thermoprocessable polyimide is to be obtained by a known method, there is almost no exception and the inherent heat resistance of the polyimide film is reduced and linear heat is applied. This leads to a significant increase in expansion coefficient (deterioration of thermal dimensional stability) (Non-patent Document 7).
従って、ポリイミドワニスを塗布乾燥するだけで(熱イミド化工程なしで)高耐熱性と低熱膨張性を有するポリイミドフィルムを得ることは原理的に極めて困難である。このような事情により、溶液加工性、耐熱性および低熱膨張性に加え、各種光学用途へ適用するため無着色透明性も保持しているポリイミドを得るための方法は知られていない。 Therefore, in principle, it is extremely difficult to obtain a polyimide film having high heat resistance and low thermal expansion by simply applying and drying a polyimide varnish (without a thermal imidization step). Under such circumstances, there is no known method for obtaining a polyimide that retains uncolored transparency for application to various optical uses in addition to solution processability, heat resistance, and low thermal expansion.
本発明は、優れた溶媒溶解性(溶液加工性)と高い耐熱性とを併せ持つ樹脂を与えるためのテトラカルボン酸二無水物、そのテトラカルボン酸二無水物から合成される溶液加工性に優れたポリイミド並びに該ポリイミドを含む溶液、および該ポリイミド並びにポリイミド溶液から得られる高い耐熱性を有するフィルムを提供することを目的とする。また、本発明は、ポリイミド共重合体と該ポリイミド共重合体を含む溶液を塗布・乾燥して得られ、高い耐熱性、低い線熱膨張係数および高い透明性を同時に有するポリイミドフィルムを提供することを目的とする。 INDUSTRIAL APPLICABILITY The present invention provides a tetracarboxylic dianhydride for providing a resin having both excellent solvent solubility (solution processability) and high heat resistance, and excellent solution processability synthesized from the tetracarboxylic dianhydride. An object is to provide a polyimide, a solution containing the polyimide, and a film having high heat resistance obtained from the polyimide and the polyimide solution. The present invention also provides a polyimide film obtained by applying and drying a polyimide copolymer and a solution containing the polyimide copolymer, and simultaneously having high heat resistance, low linear thermal expansion coefficient and high transparency. With the goal.
本発明者らは、上記課題を解決するために鋭意研究した結果、下記式(1)で表されるテトラカルボン酸二無水物から溶液加工性に優れたポリイミドが得られ、該ポリイミドを含む溶液から260℃以上の耐熱性を有するポリイミドフィルムが得られることを見出し、本発明を完成させた。 As a result of intensive studies to solve the above problems, the present inventors have obtained a polyimide having excellent solution processability from a tetracarboxylic dianhydride represented by the following formula (1), and a solution containing the polyimide From the above, it was found that a polyimide film having a heat resistance of 260 ° C. or higher was obtained, and the present invention was completed.
本発明は以下の通りである。 The present invention is as follows.
〔1〕
下記式(1):
[1]
Following formula (1):
〔2〕
下記一般式(2):
[2]
The following general formula (2):
で表される繰り返し単位を有するポリイミド。
The polyimide which has a repeating unit represented by these.
また、本発明者らは、上記式(1)で表されるテトラカルボン酸二無水物から誘導される構造を含むポリイミドの中でも特定構造を有する共重合体、即ち、下記式(5)で表される繰り返し単位及び下記一般式(6)で表される繰り返し単位を有するポリイミドの共重合体が室温で安定なポリイミド溶液を与え、これを塗布・乾燥することで、高い耐熱性、低い線熱膨張係数および高い透明性を同時に有するポリイミドフィルムが得られることを見出し、本発明を完成させた。 The present inventors also have a copolymer having a specific structure among polyimides containing a structure derived from the tetracarboxylic dianhydride represented by the above formula (1), that is, represented by the following formula (5). The polyimide copolymer having the repeating unit and the repeating unit represented by the following general formula (6) gives a stable polyimide solution at room temperature, and is coated and dried, so that it has high heat resistance and low linear heat. The inventors have found that a polyimide film having an expansion coefficient and high transparency can be obtained at the same time, and completed the present invention.
本発明は以下の通りである。 The present invention is as follows.
〔3〕
下記式(5):
[3]
Following formula (5):
下記一般式(6):
The following general formula (6):
本発明によれば、従来技術では極めて両立困難であった高い耐熱性(高ガラス転移温度)と溶媒可溶性とを併せ持つポリイミド、該ポリイミドを含む溶液から製造されるポリイミドフィルム、及び該ポリイミドを与えるためのフルオレン骨格とスピロ骨格を有するテトラカルボン酸二無水物が提供可能となる。 According to the present invention, a polyimide having both high heat resistance (high glass transition temperature) and solvent solubility, which has been extremely difficult to achieve with the prior art, a polyimide film produced from a solution containing the polyimide, and the polyimide are provided. It is possible to provide a tetracarboxylic dianhydride having a fluorene skeleton and a spiro skeleton.
更には、前記ポリイミドの中から特定構造を有する共重合体を選択することによって、高い耐熱性・高い透明性に加え低熱膨張性をも兼ね備えるポリイミドフィルムが提供可能となる。 Furthermore, by selecting a copolymer having a specific structure from among the polyimides, it is possible to provide a polyimide film having both low heat expansion and high heat resistance and high transparency.
<テトラカルボン酸二無水物>
本発明のテトラカルボン酸二無水物は、以下式(1)で表される構造を有する。
<Tetracarboxylic dianhydride>
The tetracarboxylic dianhydride of the present invention has a structure represented by the following formula (1).
<ポリイミド>
本発明にかかる式(1)で表されるテトラカルボン酸二無水物の構造的特徴は、キサンテン構造とフルオレン構造が直交したスピロ構造を有し、無水フタル酸部位がエステル結合を介しキサンテン構造に結合している点にある。
<Polyimide>
The structural characteristics of the tetracarboxylic dianhydride represented by the formula (1) according to the present invention include a spiro structure in which the xanthene structure and the fluorene structure are orthogonal to each other, and the phthalic anhydride moiety is converted to the xanthene structure via an ester bond. It is at the point where it joins.
本発明にかかる下記式(2)で表されるポリイミドは、上記式(1)で表されるテトラカルボン酸二無水物を原料とすることで、上述した特異な物性を有する有用なポリイミドを得ることができる。その製造方法については特に限定されないが、例えば、上記式(1)で表されるテトラカルボン酸二無水物と、2価の求核反応性官能基をもつ芳香族または脂肪族化合物を反応させて下記式(2)で表される繰り返し単位を有するポリイミドの前駆体を得た後、イミド化する工程を経る二段階合成法、または高沸点溶媒中、上記式(1)で表されるテトラカルボン酸二無水物と2価の求核反応性官能基をもつ芳香族または脂肪族化合物を150~220℃で撹拌しながら反応させる一段階合成法がある。 The polyimide represented by the following formula (2) according to the present invention uses the tetracarboxylic dianhydride represented by the above formula (1) as a raw material to obtain a useful polyimide having the above-mentioned specific physical properties. be able to. The production method is not particularly limited. For example, the tetracarboxylic dianhydride represented by the above formula (1) is reacted with an aromatic or aliphatic compound having a divalent nucleophilic reactive functional group. After obtaining a polyimide precursor having a repeating unit represented by the following formula (2), a tetracarboxylic acid represented by the above formula (1) in a two-step synthesis method through a process of imidization or in a high boiling point solvent There is a one-step synthesis method in which an dianhydride and an aromatic or aliphatic compound having a divalent nucleophilic reactive functional group are reacted at 150 to 220 ° C. with stirring.
本発明のポリイミドは、以下式(2)で表される構造を有する。 The polyimide of the present invention has a structure represented by the following formula (2).
上記式(2)中、Xで表される2価の芳香族または脂肪族基は、後述する上記式(1)で表されるテトラカルボン酸二無水物と反応させる、2価の求核反応性官能基を有する芳香族または脂肪族化合物の骨格構造を表す。なお、本発明における2価の求核反応性官能基としてはアミノ基、イソシアナート基等が例示される。
In the above formula (2), a divalent aromatic or aliphatic group represented by X is reacted with a tetracarboxylic dianhydride represented by the above formula (1) described later. Represents a skeleton structure of an aromatic or aliphatic compound having a functional group. In addition, an amino group, an isocyanate group, etc. are illustrated as a bivalent nucleophilic reactive functional group in this invention.
2価の求核反応性官能基をもつ芳香族または脂肪族化合物として具体的に例えば、ジアミン類として、p-フェニレンジアミン、m-フェニレンジアミン、4,4’-ビス(4-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)スルホン、ビス(4-(4-アミノフェノキシ)フェニル)スルホン、2,2-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)ヘキサフルオロプロパン、2,2-ビス(4-アミノフェニル)ヘキサフルオロプロパン、p-ターフェニレンジアミン、ベンジジン、3,3’-ジヒドロキシベンジジン、3,3’-ジメトキシベンジジン、o-トリジン、m-トリジン、4,4’‐ジアミノ-2,2’‐ビス(トリフルオロメチル)ビフェニル、1,4-ビス(4-アミノフェノキシ)ベンゼン、1,3-ビス(4-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、4,4’-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、3,3’-ジアミノジフェニルエーテル、2,4’-ジアミノジフェニルエーテル、4,4’-ジアミノジフェニルスルホン、3,3’-ジアミノジフェニルスルホン、4,4’-ジアミノベンゾフェノン、3,3’-ジアミノベンゾフェノン、4,4’-ジアミノベンズアニリド、4-アミノフェニル-4’-アミノベンゾエート、2,4-ジアミノトルエン、2,5-ジアミノトルエン、2,4-ジアミノキシレン、2,4-ジアミノデュレン、4,4’-ジアミノジフェニルメタン、4,4’-メチレンビス(2-メチルアニリン)、4,4’-メチレンビス(2-エチルアニリン)、4,4’-メチレンビス(2,6-ジメチルアニリン)、4,4’-メチレンビス(2,6-ジエチルアニリン)等の芳香族ジアミン、4,4’-メチレンビス(シクロヘキシルアミン)、イソホロンジアミン、トランス-1,4-ジアミノシクロヘキサン、シス-1,4-ジアミノシクロヘキサン、1,4-シクロヘキサンビス(メチルアミン)、2,5-ビス(アミノメチル)ビシクロ〔2.2.1〕ヘプタン、2,6-ビス(アミノメチル)ビシクロ〔2.2.1〕ヘプタン、3,8-ビス(アミノメチル)トリシクロ〔5.2.1.0〕デカン、1,3-ジアミノアダマンタン、2,2-ビス(4-アミノシクロヘキシル)プロパン、2,2-ビス(4-アミノシクロヘキシル)ヘキサフルオロプロパン等の脂環式ジアミン、1,3-プロパンジアミン、1,4-テトラメチレンジアミン、1,5-ペンタメチレンジアミン、1,6-ヘキサメチレンジアミン、1,7-ヘプタメチレンジアミン、1,8-オクタメチレンジアミン、1,9-ノナメチレンジアミン、ジアミノシロキサン等の鎖状脂肪族ジアミンが挙げられる。また、ジイソシアナート類としては、1,5-フェニレンジイソシアナート、1,3-ジイソシアナトベンゼン、3,3'-ジクロロ-4,4'-ジイソシアナトビフェニル、4,4'-ジイソシアナト-3,3'-ジメチルジフェニルメタン、1,5-ジイソシアナトナフタレン、トリレン-2,6-ジイソシアナート、m-キシリレンジイソシアナート、2,2-ビス(4-イソシアナトフェニル)ヘキサフルオロプロパン等の芳香族ジイソシアナート、ジシクロヘキシルメタン4,4’-ジイソシアナート等の脂環式ジイソシアナート、ヘキサメチレンジイソシアナート等の鎖状脂肪族ジイソシアナートが挙げられる。また、これらを2種類以上併用することもできる。 Specific examples of aromatic or aliphatic compounds having a divalent nucleophilic reactive functional group include, for example, p-phenylenediamine, m-phenylenediamine, 4,4′-bis (4-aminophenoxy) biphenyl as diamines. Bis (4- (3-aminophenoxy) phenyl) sulfone, bis (4- (4-aminophenoxy) phenyl) sulfone, 2,2-bis (4- (4-aminophenoxy) phenyl) propane, 2,2 -Bis (4- (4-aminophenoxy) phenyl) hexafluoropropane, 2,2-bis (4-aminophenyl) hexafluoropropane, p-terphenylenediamine, benzidine, 3,3'-dihydroxybenzidine, 3, 3'-dimethoxybenzidine, o-tolidine, m-tolidine, 4,4'-diamino-2,2'-bis (to Fluoromethyl) biphenyl, 1,4-bis (4-aminophenoxy) benzene, 1,3-bis (4-aminophenoxy) benzene, 1,3-bis (3-aminophenoxy) benzene, 4,4'-diamino Diphenyl ether, 3,4'-diaminodiphenyl ether, 3,3'-diaminodiphenyl ether, 2,4'-diaminodiphenyl ether, 4,4'-diaminodiphenyl sulfone, 3,3'-diaminodiphenyl sulfone, 4,4'-diamino Benzophenone, 3,3'-diaminobenzophenone, 4,4'-diaminobenzanilide, 4-aminophenyl-4'-aminobenzoate, 2,4-diaminotoluene, 2,5-diaminotoluene, 2,4-diaminoxylene 2,4-diaminodurene, 4,4'-diaminodi Phenylmethane, 4,4'-methylenebis (2-methylaniline), 4,4'-methylenebis (2-ethylaniline), 4,4'-methylenebis (2,6-dimethylaniline), 4,4'-methylenebis Aromatic diamines such as (2,6-diethylaniline), 4,4′-methylenebis (cyclohexylamine), isophoronediamine, trans-1,4-diaminocyclohexane, cis-1,4-diaminocyclohexane, 1,4- Cyclohexanebis (methylamine), 2,5-bis (aminomethyl) bicyclo [2.2.1] heptane, 2,6-bis (aminomethyl) bicyclo [2.2.1] heptane, 3,8-bis (Aminomethyl) tricyclo [5.2.1.0] decane, 1,3-diaminoadamantane, 2,2-bis (4-aminocyclohexane) Sil) propane, 2,2-bis (4-aminocyclohexyl) hexafluoropropane and other alicyclic diamines, 1,3-propanediamine, 1,4-tetramethylenediamine, 1,5-pentamethylenediamine, 1, Examples thereof include chain aliphatic diamines such as 6-hexamethylenediamine, 1,7-heptamethylenediamine, 1,8-octamethylenediamine, 1,9-nonamethylenediamine, and diaminosiloxane. The diisocyanates include 1,5-phenylene diisocyanate, 1,3-diisocyanatobenzene, 3,3′-dichloro-4,4′-diisocyanatobiphenyl, and 4,4′-diisocyanate. -3,3'-dimethyldiphenylmethane, 1,5-diisocyanatonaphthalene, tolylene-2,6-diisocyanate, m-xylylene diisocyanate, 2,2-bis (4-isocyanatophenyl) hexafluoropropane Aromatic diisocyanates such as dicyclomethane, alicyclic diisocyanates such as dicyclohexylmethane 4,4′-diisocyanate, and chain aliphatic diisocyanates such as hexamethylene diisocyanate. Two or more of these may be used in combination.
本発明にかかるポリイミドを重合する際の重合反応性およびポリイミドの特性を著しく損なわない範囲で、上記式(1)で表されるテトラカルボン酸二無水物以外の芳香族または脂肪族テトラカルボン酸二無水物を共重合成分として併用できる。その際に使用可能な芳香族テトラカルボン酸二無水物として例えば、ピロメリット酸二無水物、3,4,3’,4’-ビフェニルテトラカルボン酸二無水物、2,3,3’,4’-ビフェニルテトラカルボン酸二無水物、2,3,2’,3’-ビフェニルテトラカルボン酸二無水物、ハイドロキノン-ビス(トリメリテートアンハイドライド)、メチルハイドロキノン-ビス(トリメリテートアンハイドライド)、1,4,5,8-ナフタレンテトラカルボン酸二無水物、2,3,6,7-ナフタレンテトラカルボン酸二無水物、3,4,3’,4’-ベンゾフェノンテトラカルボン酸二無水物、2,3,3’,4’-ベンゾフェノンテトラカルボン酸二無水物、2,3,2’,3’-ベンゾフェノンテトラカルボン酸二無水物、3,4,3’,4’-ビフェニルエーテルテトラカルボン酸二無水物、3,4,2’,3’-ビフェニルエーテルテトラカルボン酸二無水物、2,3,2’,3’-ビフェニルエーテルテトラカルボン酸二無水物、3,4,3’,4’-ビフェニルスルホンテトラカルボン酸二無水物、3,4,2’,3’-ビフェニルスルホンテトラカルボン酸二無水物、2,3,2’,3’-ビフェニルスルホンテトラカルボン酸二無水物、2,2’-ビス(3,4-ジカルボキシフェニル)ヘキサフルオロプロパン酸二無水物、2,2’-ビス(3,4-ジカルボキシフェニル)プロパン酸二無水物等が挙げられる。脂肪族テトラカルボン酸二無水物としては、特に限定されないが、例えば、脂環式のものとしては、ビシクロ[2.2.2]オクト-7-エン-2,3,5,6-テトラカルボン酸二無水物、5-(ジオキソテトラヒドロフリル-3-メチル-3-シクロヘキセン-1,2-ジカルボン酸無水物、4-(2,5-ジオキソテトラヒドロフラン-3-イル)テトラリン-1,2-ジカルボン酸無水物、テトラヒドロフラン-2,3,4,5-テトラカルボン酸二無水物、ビシクロ-3,3’,4,4’-テトラカルボン酸二無水物、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-シクロペンタンテトラカルボン酸二無水物等が挙げられる。また、これらを2種類以上併用することもできる。 Aromatic or aliphatic tetracarboxylic acid other than the tetracarboxylic dianhydride represented by the above formula (1) within a range that does not significantly impair the polymerization reactivity and the characteristics of the polyimide when polymerizing the polyimide according to the present invention. An anhydride can be used in combination as a copolymerization component. Examples of aromatic tetracarboxylic dianhydrides that can be used in this case include pyromellitic dianhydride, 3,4,3 ′, 4′-biphenyltetracarboxylic dianhydride, 2,3,3 ′, 4. '-Biphenyltetracarboxylic dianhydride, 2,3,2', 3'-biphenyltetracarboxylic dianhydride, hydroquinone-bis (trimellitate anhydride), methylhydroquinone-bis (trimellitate anhydride) 1,4,5,8-naphthalenetetracarboxylic dianhydride, 2,3,6,7-naphthalenetetracarboxylic dianhydride, 3,4,3 ′, 4′-benzophenonetetracarboxylic dianhydride 2,3,3 ′, 4′-benzophenone tetracarboxylic dianhydride, 2,3,2 ′, 3′-benzophenone tetracarboxylic dianhydride, 3,4,3 , 4′-biphenyl ether tetracarboxylic dianhydride, 3,4,2 ′, 3′-biphenyl ether tetracarboxylic dianhydride, 2,3,2 ′, 3′-biphenyl ether tetracarboxylic dianhydride 3,4,3 ′, 4′-biphenylsulfonetetracarboxylic dianhydride, 3,4,2 ′, 3′-biphenylsulfonetetracarboxylic dianhydride, 2,3,2 ′, 3′-biphenyl Sulfonetetracarboxylic dianhydride, 2,2'-bis (3,4-dicarboxyphenyl) hexafluoropropanoic dianhydride, 2,2'-bis (3,4-dicarboxyphenyl) propanoic dianhydride Thing etc. are mentioned. The aliphatic tetracarboxylic dianhydride is not particularly limited. For example, as the alicyclic one, bicyclo [2.2.2] oct-7-ene-2,3,5,6-tetracarboxylic Acid dianhydride, 5- (dioxotetrahydrofuryl-3-methyl-3-cyclohexene-1,2-dicarboxylic acid anhydride, 4- (2,5-dioxotetrahydrofuran-3-yl) tetralin-1,2 -Dicarboxylic anhydride, tetrahydrofuran-2,3,4,5-tetracarboxylic dianhydride, bicyclo-3,3 ', 4,4'-tetracarboxylic dianhydride, 1,2,3,4 Examples thereof include cyclobutanetetracarboxylic dianhydride, 1,2,3,4-cyclopentanetetracarboxylic dianhydride, etc. Two or more of these may be used in combination.
本発明にかかるポリイミドまたはポリアミド酸を合成する際の溶媒としては、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-メチル-2-ピロリドン、ジメチルスルホオキシド等の非プロトン性溶媒が好ましいが、原料と生成するポリイミド前駆体、そしてイミド化されたポリイミドが溶解し、原料や生成物と反応しないものであればどのような溶媒であっても何ら問題なく使用でき、特にその溶媒の種類に限定されない。 As the solvent for synthesizing the polyimide or polyamic acid according to the present invention, aprotic solvents such as N, N-dimethylformamide, N, N-dimethylacetamide, N-methyl-2-pyrrolidone, dimethyl sulfoxide and the like are preferable. However, any solvent can be used without any problem as long as the raw material, the polyimide precursor to be produced, and the imidized polyimide are dissolved and do not react with the raw material or the product. It is not limited to.
具体的に例えば、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-メチル-2-ピロリドン等のアミド溶媒、γ-ブチロラクトン、γ-バレロラクトン、δ-バレロラクトン、γ-カプロラクトン、ε-カプロラクトン、α-メチル-γ-ブチロラクトン、酢酸ブチル、酢酸エチル、酢酸イソブチル等のエステル溶媒、エチレンカーボネート、プロピレンカーボネート等のカーボネート溶媒、ジエチレングリコールジメチルエーテル、トリエチレングリコール、トリエチレングリコールジメチルエーテル等のグリコール系溶媒、フェノール、m-クレゾール、p-クレゾール、o-クレゾール、3-クロロフェノール、4-クロロフェノール等のフェノール系溶媒、シクロペンタノン、シクロヘキサノン、アセトン、メチルエチルケトン、ジイソブチルケトン、メチルイソブチルケトン等のケトン系溶媒、テトラヒドロフラン、1,4-ジオキサン、ジメトキシエタン、ジエトキシエタン、ジブチルエーテル等のエーテル系溶媒、その他汎用溶媒として、アセトフェノン、1,3-ジメチル-2-イミダゾリジノン、スルホラン、ジメチルスルホキシド、プロピレングリコールメチルアセテート、エチルセロソルブ、ブチルセロソルブ、2-メチルセロソルブアセテート、エチルセロソルブアセテート、ブチルセロソルブアセテート、ブタノール、エタノール、キシレン、トルエン、クロルベンゼン、ターペン、ミネラルスピリット、石油ナフサ系溶媒などが使用でき、これらを2種類以上混合して用いてもよい。 Specifically, for example, amide solvents such as N, N-dimethylformamide, N, N-dimethylacetamide, N-methyl-2-pyrrolidone, γ-butyrolactone, γ-valerolactone, δ-valerolactone, γ-caprolactone, ε -Ester solvents such as caprolactone, α-methyl-γ-butyrolactone, butyl acetate, ethyl acetate and isobutyl acetate, carbonate solvents such as ethylene carbonate and propylene carbonate, glycol solvents such as diethylene glycol dimethyl ether, triethylene glycol and triethylene glycol dimethyl ether Phenol solvents such as phenol, m-cresol, p-cresol, o-cresol, 3-chlorophenol, 4-chlorophenol, cyclopentanone, cyclohexanone, acetone, methyl Ketone solvents such as ethyl ketone, diisobutyl ketone and methyl isobutyl ketone, ether solvents such as tetrahydrofuran, 1,4-dioxane, dimethoxyethane, diethoxyethane and dibutyl ether, and other general-purpose solvents include acetophenone, 1,3-dimethyl- 2-imidazolidinone, sulfolane, dimethyl sulfoxide, propylene glycol methyl acetate, ethyl cellosolve, butyl cellosolve, 2-methyl cellosolve acetate, ethyl cellosolve acetate, butanol, ethanol, xylene, toluene, chlorobenzene, terpene, mineral spirit, Petroleum naphtha solvents can be used, and two or more of these may be used in combination.
本発明の式(1)で表されるテトラカルボン酸二無水物を合成する方法は特に限定されず、公知のエステル化反応を適宜用いることができる。具体的には、例えば、無水トリメリット酸クロリドを脱水非プロトン性溶媒に溶解させ、式(3)のジオールと脱酸剤を同様の溶媒に溶解させた溶液を、メカニカルスターラー等を用いて、温度-78℃~0℃の範囲、好ましくは-30℃~-5℃で加え、0.5~48時間、好ましくは1~24時間撹拌する。その後、反応溶液を0~100℃、好ましくは10~50℃まで昇温させ0.5~48時間、好ましくは1~24時間撹拌し、エステル化を完結させる。続いて、生成物を含む溶液から生成物を単離し、適宜洗浄し、真空乾燥器等で20~220℃、より好ましくは50~200℃で乾燥させ、本発明の式(1)で表されるテトラカルボン酸二無水物を得ることができる。本発明の式(1)で表されるテトラカルボン酸二無水物の純度が低い場合は、公知の方法、例えば昇華法や再結晶法で適宜精製できる。 The method for synthesizing the tetracarboxylic dianhydride represented by the formula (1) of the present invention is not particularly limited, and a known esterification reaction can be appropriately used. Specifically, for example, a solution in which trimellitic anhydride chloride is dissolved in a dehydrated aprotic solvent and a diol of formula (3) and a deoxidizing agent are dissolved in the same solvent, using a mechanical stirrer or the like, Add in the temperature range of −78 ° C. to 0 ° C., preferably −30 ° C. to −5 ° C. and stir for 0.5 to 48 hours, preferably 1 to 24 hours. Thereafter, the reaction solution is heated to 0 to 100 ° C., preferably 10 to 50 ° C., and stirred for 0.5 to 48 hours, preferably 1 to 24 hours to complete the esterification. Subsequently, the product is isolated from the solution containing the product, washed as appropriate, and dried at 20 to 220 ° C., more preferably at 50 to 200 ° C. with a vacuum dryer or the like, and is represented by the formula (1) of the present invention. Tetracarboxylic dianhydride can be obtained. When the purity of the tetracarboxylic dianhydride represented by the formula (1) of the present invention is low, it can be appropriately purified by a known method such as a sublimation method or a recrystallization method.
本発明の上記式(2)で表されるポリイミド及び該ポリイミドを含む溶液を合成する方法は、特に限定されず、公知のイミド化反応を適宜用いることができる。 The method for synthesizing the polyimide represented by the above formula (2) of the present invention and the solution containing the polyimide is not particularly limited, and a known imidization reaction can be appropriately used.
具体的には、例えば、以下の一段階法で合成できる。2価の求核反応性官能基がイソシアナート基の場合、芳香族または脂肪族ジイソシアナートを溶媒に溶解させ、この溶液にジイソシアナート基と等モルの式(1)で表されるテトラカルボン酸二無水物の粉末を徐々に、または分割して加え、メカニカルスターラー等を用いて、温度-20~100℃の範囲、より好ましくは、0~50℃で0.5~168時間、より好ましくは1~72時間撹拌することで、上記式(2)で表されるポリイミドを含む溶液が得られる。 Specifically, for example, it can be synthesized by the following one-step method. When the divalent nucleophilic reactive functional group is an isocyanate group, an aromatic or aliphatic diisocyanate is dissolved in a solvent, and the tetraisocyanate represented by the formula (1) is equimolar with the diisocyanate group. Add the carboxylic acid dianhydride powder gradually or in portions and use a mechanical stirrer or the like in the temperature range of −20 to 100 ° C., more preferably 0 to 50 ° C. for 0.5 to 168 hours, The solution containing the polyimide represented by the above formula (2) is preferably obtained by stirring for 1 to 72 hours.
また、2価の求核反応性官能基がアミノ基の場合、芳香族または脂肪族ジアミンを高沸点溶媒に溶解させ、この溶液にジアミンと等モルの式(1)で表されるテトラカルボン酸二無水物の粉末を徐々に、または分割して加えた後、トルエンなどの共沸剤を加え、不活性ガスを導入しながら150~220℃、より好ましくは、160~190℃でメカニカルスターラー等を用いて0.5~10時間、より好ましくは1~5時間で撹拌し、イミド化時に生成する水を共沸剤とともに系外に除去することでイミド化でき、室温に戻すだけで上記式(2)で表されるポリイミドを含む溶液を得ることができる。尚、イミド化反応の副生成物である水や共沸剤を除去する際に、反応容器内を減圧にすることも可能であり、この工程により固形分濃度を高めることもできる。 Further, when the divalent nucleophilic reactive functional group is an amino group, an aromatic or aliphatic diamine is dissolved in a high boiling point solvent, and the tetracarboxylic acid represented by the formula (1) is equimolar with the diamine. After the dianhydride powder is added gradually or in portions, an azeotropic agent such as toluene is added, and an inert gas is introduced at 150 to 220 ° C., more preferably at 160 to 190 ° C. For 0.5 to 10 hours, more preferably 1 to 5 hours, and imidation can be achieved by removing the water produced during imidization out of the system together with the azeotropic agent. A solution containing the polyimide represented by (2) can be obtained. In addition, when removing the water and the azeotropic agent which are by-products of the imidation reaction, the inside of the reaction vessel can be reduced in pressure, and the solid content concentration can be increased by this step.
また、本発明の上記式(2)で表されるポリイミド及び該ポリイミドを含む溶液は以下の二段階法を用いても合成できる。2価の求核反応性官能基がアミノ基の場合、まず、第一段階目として、芳香族または脂肪族ジアミンを溶媒に溶解させ、この溶液にジアミンと等モルの式(1)で表されるテトラカルボン酸二無水物の粉末を徐々に、または分割して加え、メカニカルスターラー等を用いて、温度0~100℃の範囲、より好ましくは、5~50℃で0.5~168時間、より好ましくは1~96時間撹拌することで、ポリイミド前駆体であるポリアミド酸溶液が得られる。この際の固形分濃度は、ポリアミド酸の分子量を最大限に高めるため、溶液が均一となり撹拌できる最大濃度が望ましい。即ち、固形分濃度は1~50重量%、より好ましくは5~40重量%である。このような固形分濃度であれば、生成するポリアミド酸の重合度が十分高くなる。また、脂肪族ジアミンを使用した場合、重合初期にしばしば塩形成が起こり、重合が妨害されるが、塩形成を抑制しつつできるだけ重合度を上げるためには、重合時の固形分濃度を上記の好適な濃度範囲に管理することが好ましい。 Further, the polyimide represented by the above formula (2) of the present invention and the solution containing the polyimide can also be synthesized using the following two-step method. When the divalent nucleophilic reactive functional group is an amino group, first, as a first step, an aromatic or aliphatic diamine is dissolved in a solvent, and this solution is represented by the formula (1) equimolar with the diamine. Tetracarboxylic dianhydride powder is added gradually or in portions, and a temperature of 0 to 100 ° C., more preferably 5 to 50 ° C. for 0.5 to 168 hours, using a mechanical stirrer or the like, More preferably, the polyamic acid solution which is a polyimide precursor is obtained by stirring for 1 to 96 hours. In this case, the solid concentration is preferably the maximum concentration at which the solution becomes uniform and can be stirred in order to maximize the molecular weight of the polyamic acid. That is, the solid content concentration is 1 to 50% by weight, more preferably 5 to 40% by weight. With such a solid content concentration, the degree of polymerization of the produced polyamic acid is sufficiently high. In addition, when an aliphatic diamine is used, salt formation often occurs at the initial stage of polymerization and the polymerization is hindered, but in order to increase the degree of polymerization as much as possible while suppressing salt formation, the solid content concentration during the polymerization is It is preferable to manage within a suitable concentration range.
次いで、第二段階目として前記で得られたポリイミド前駆体、即ちポリアミド酸をイミド化する方法について説明する。本発明のポリイミドを得るためには、熱的に脱水閉環する高温溶液イミド化法、脱水剤を用いる化学イミド化法などの公知の方法が適宜使用できる。 Next, a method for imidizing the polyimide precursor obtained above, that is, polyamic acid, will be described as the second stage. In order to obtain the polyimide of this invention, well-known methods, such as the high temperature solution imidation method thermally dehydrated and closed and the chemical imidation method using a dehydrating agent, can be used suitably.
具体的には、例えば、高温溶液イミド化法を適用する場合は、高沸点溶媒中で合成した前記方法で得られたポリアミド酸溶液に、上述したポリアミド酸を製造する際に使用可能な溶媒、特に前記ポリアミド酸製造時に用いた溶媒と同一の溶媒を加えて撹拌し易い適度な溶液粘度とし、更にトルエンなどの共沸剤を加え、不活性ガスを導入しながら150~220℃、より好ましくは、160~190℃でメカニカルスターラー等を用いて0.5~10時間、より好ましくは1~5時間、撹拌し、イミド化時に生成する水を共沸剤とともに系外に除去することで容易にイミド化でき、これを室温に戻すだけで上記式(2)で表されるポリイミド含む溶液を得ることができる。尚、イミド化時に副生成物である水や共沸剤を除去する際に、反応容器内を減圧にすることも可能であり、これにより固形分濃度を高めることもできる。 Specifically, for example, when applying a high temperature solution imidization method, a solvent that can be used in producing the above-described polyamic acid to the polyamic acid solution obtained by the above method synthesized in a high boiling point solvent, In particular, the same solvent as that used in the preparation of the polyamic acid is added to obtain an appropriate solution viscosity that is easy to stir. Further, an azeotropic agent such as toluene is added, and 150 to 220 ° C., more preferably while introducing an inert gas. , By stirring at 160 to 190 ° C. using a mechanical stirrer for 0.5 to 10 hours, more preferably 1 to 5 hours, and easily removing water generated during imidization together with the azeotropic agent from the system. A solution containing polyimide represented by the above formula (2) can be obtained by imidization and simply returning the temperature to room temperature. In addition, when removing water and an azeotropic agent which are by-products at the time of imidation, it is possible to reduce the pressure in the reaction vessel, thereby increasing the solid content concentration.
また、化学イミド化法を適用する場合は、前記方法で得られたポリアミド酸溶液に上述したポリアミド酸を製造する際に使用可能な溶媒、特に前記ポリアミド酸製造時に用いた溶媒と同一の溶媒を加えて撹拌し易い適度な溶液粘度とし、メカニカルスターラーなどで撹拌しながら、有機酸の無水物と、塩基性触媒として3級アミンからなる脱水閉環剤(化学イミド化剤)を滴下し、温度0~100℃、好ましくは10~50℃で1~72時間撹拌することで化学的にイミド化を完結させることができる。その際に使用可能な有機酸無水物としては、特に限定されないが、無水酢酸、無水プロピオン酸等が挙げられる。試薬の取り扱いや分離のし易さから無水酢酸が好適に使用される。また塩基性触媒としては、ピリジン、トリエチルアミン、キノリン等が使用できるが試薬の取り扱いや分離のし易さからピリジンが好適に用いられるが、これらに限定されない。化学イミド化剤中の有機酸無水物量は、ポリアミド酸の理論脱水量の1~20倍モルの範囲であり、より好ましくは1~10倍モルである。また塩基性触媒の量は、有機酸無水物量に対して0.1~2倍モルの範囲であり、より好ましくは0.1~1倍モルの範囲である。 In addition, when applying the chemical imidization method, a solvent that can be used for producing the above-described polyamic acid to the polyamic acid solution obtained by the above-described method, in particular, the same solvent as that used for producing the polyamic acid is used. In addition, the solution viscosity is set to an appropriate level that is easy to stir, and while stirring with a mechanical stirrer or the like, an organic acid anhydride and a dehydrating cyclization agent (chemical imidization agent) composed of a tertiary amine as a basic catalyst are dropped. The imidization can be completed chemically by stirring at -100 ° C, preferably 10-50 ° C, for 1-72 hours. Although it does not specifically limit as an organic acid anhydride which can be used in that case, An acetic anhydride, propionic anhydride, etc. are mentioned. Acetic anhydride is preferably used because of easy handling and separation of the reagent. As the basic catalyst, pyridine, triethylamine, quinoline and the like can be used, but pyridine is preferably used because of easy handling and separation of the reagent, but is not limited thereto. The amount of the organic acid anhydride in the chemical imidizing agent is in the range of 1 to 20 times mol, more preferably 1 to 10 times mol of the theoretical dehydration amount of the polyamic acid. The amount of the basic catalyst is in the range of 0.1 to 2 moles, more preferably in the range of 0.1 to 1 moles, relative to the amount of the organic acid anhydride.
前記化学イミド化法で得られた反応溶液中には、塩基や未反応の化学イミド化剤、有機酸などの副生成物(以下、不純物という)が混入しているため、これらを除去してポリイミドを単離・精製してもよい。精製は公知の方法が利用できる。例えば、最も簡便な方法としては、イミド化した反応溶液を撹拌しながら大量の貧溶媒中に滴下してポリイミドを析出させた後、ポリイミド粉末を回収して不純物が除去されるまで繰返し洗浄し、減圧乾燥して、ポリイミド粉末を得る方法が適用できる。この時、使用できる溶媒としては、ポリイミドを析出させ、不純物を効率よく除去でき、乾燥し易い溶媒であれば特に限定されないが、例えば、水をはじめ、メタノール、エタノール、イソプロパノールなどのアルコール類が好適であり、これらを混合して用いてもよい。貧溶媒中に滴下して析出させる時のポリイミド溶液の固形分濃度は、高すぎると析出するポリイミドが粒塊となり、その粗大な粒子中に不純物が残留する場合や、得られたポリイミド粉末を溶媒に再溶解する際に長時間要する場合がある。一方、ポリイミド溶液の濃度を薄くし過ぎると、多量の貧溶媒が必要となり、廃溶剤処理による環境負荷増大や製造コスト高になる場合がある。したがって、貧溶媒中に滴下する時のポリイミド溶液の濃度(固形分濃度)は、20重量%以下、より好ましくは10重量%以下である。この時使用する貧溶媒の量はポリイミド溶液中の溶媒やポリイミドの種類に応じて当業者であれば適宜調整可能である。前述のように析出させたポリイミド粉末は回収し、残留溶媒を真空乾燥や熱風乾燥などで除去する。乾燥温度と時間は、ポリイミドが変質しない温度であれば制限はなく、温度30~150℃で3~24時間乾燥させることが好ましい。 In the reaction solution obtained by the chemical imidization method, by-products (hereinafter referred to as impurities) such as bases, unreacted chemical imidization agents, and organic acids are mixed. Polyimide may be isolated and purified. A known method can be used for purification. For example, as the simplest method, after dripping in a large amount of poor solvent while stirring the imidized reaction solution to precipitate polyimide, the polyimide powder is recovered and repeatedly washed until impurities are removed, A method of obtaining polyimide powder by drying under reduced pressure can be applied. At this time, the solvent that can be used is not particularly limited as long as it can precipitate polyimide, efficiently remove impurities, and can be easily dried. For example, water, alcohols such as methanol, ethanol, and isopropanol are preferable. These may be used in combination. When the solid content concentration of the polyimide solution when dropped in a poor solvent is too high, the precipitated polyimide becomes agglomerates and impurities remain in the coarse particles, or the obtained polyimide powder is used as a solvent. It may take a long time to redissolve. On the other hand, if the concentration of the polyimide solution is too thin, a large amount of poor solvent is required, which may increase the environmental load and increase the manufacturing cost due to waste solvent treatment. Therefore, the concentration (solid content concentration) of the polyimide solution when dripped in the poor solvent is 20% by weight or less, more preferably 10% by weight or less. The amount of the poor solvent used at this time can be appropriately adjusted by those skilled in the art depending on the type of solvent and polyimide in the polyimide solution. The polyimide powder deposited as described above is collected, and the residual solvent is removed by vacuum drying or hot air drying. The drying temperature and time are not limited as long as the polyimide does not change in quality, and it is preferable to dry at a temperature of 30 to 150 ° C. for 3 to 24 hours.
このようにして得られた上記式(2)で表されるポリイミド粉末は、ポリイミド溶液とするために溶媒に溶解させる必要がある。使用可能な溶媒は、ポリアミド酸溶液の使用用途や加工条件に合わせて適宜選択可能である。具体的には例えば、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-メチル-2-ピロリドン等のアミド溶媒、γ-ブチロラクトン、γ-バレロラクトン、δ-バレロラクトン、γ-カプロラクトン、ε-カプロラクトン、α-メチル-γ-ブチロラクトン、酢酸ブチル、酢酸エチル、酢酸イソブチル等のエステル溶媒、エチレンカーボネート、プロピレンカーボネート等のカーボネート溶媒、ジエチレングリコールジメチルエーテル、トリエチレングリコール、トリエチレングリコールジメチルエーテル等のグリコール系溶媒、フェノール、m-クレゾール、p-クレゾール、o-クレゾール、3-クロロフェノール、4-クロロフェノール等のフェノール系溶媒、シクロペンタノン、シクロヘキサノン、アセトン、メチルエチルケトン、ジイソブチルケトン、メチルイソブチルケトン等のケトン系溶媒、テトラヒドロフラン、1,4-ジオキサン、ジメトキシエタン、ジエトキシエタン、ジブチルエーテル等のエーテル系溶媒、その他汎用溶媒として、アセトフェノン、1,3-ジメチル-2-イミダゾリジノン、スルホラン、ジメチルスルホキシド、プロピレングリコールメチルアセテート、エチルセロソルブ、ブチルセロソルブ、2-メチルセロソルブアセテート、エチルセロソルブアセテート、ブチルセロソルブアセテート、ブタノール、エタノール、キシレン、トルエン、クロルベンゼン、ターペン、ミネラルスピリット、石油ナフサ系溶媒なども使用でき、これらを2種類以上混合して用いてもよい。 The polyimide powder represented by the above formula (2) thus obtained needs to be dissolved in a solvent in order to obtain a polyimide solution. The solvent that can be used can be appropriately selected according to the intended use and processing conditions of the polyamic acid solution. Specifically, for example, amide solvents such as N, N-dimethylformamide, N, N-dimethylacetamide, N-methyl-2-pyrrolidone, γ-butyrolactone, γ-valerolactone, δ-valerolactone, γ-caprolactone, ε-caprolactone, α-methyl-γ-butyrolactone, ester solvents such as butyl acetate, ethyl acetate and isobutyl acetate, carbonate solvents such as ethylene carbonate and propylene carbonate, glycols such as diethylene glycol dimethyl ether, triethylene glycol and triethylene glycol dimethyl ether Solvent, phenol solvents such as phenol, m-cresol, p-cresol, o-cresol, 3-chlorophenol, 4-chlorophenol, cyclopentanone, cyclohexanone, acetone, methyl Ketone solvents such as ethyl ketone, diisobutyl ketone and methyl isobutyl ketone, ether solvents such as tetrahydrofuran, 1,4-dioxane, dimethoxyethane, diethoxyethane and dibutyl ether, and other general-purpose solvents include acetophenone, 1,3-dimethyl- 2-imidazolidinone, sulfolane, dimethyl sulfoxide, propylene glycol methyl acetate, ethyl cellosolve, butyl cellosolve, 2-methyl cellosolve acetate, ethyl cellosolve acetate, butanol, ethanol, xylene, toluene, chlorobenzene, terpene, mineral spirit, Petroleum naphtha solvents can also be used, and two or more of these may be used in combination.
特に、長時間にわたり連続塗工する場合、ポリイミド溶液中の溶媒が大気中の水分を吸湿し、ポリイミドが析出する恐れがある場合は、トリエチレングリコールジメチルエーテル、γ-ブチロラクトンあるいはシクロペンタノンなどの低吸湿性溶媒を使用することが好ましい。また、吸湿性溶媒である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-メチル-2-ピロリドン等のアミド溶媒でも、上記低吸湿性溶媒と組み合わせることで、ポリイミドの析出を抑制することもできる。ポリイミド粉末の溶解方法は、空気中、または不活性ガス中で室温~溶媒の沸点以下の温度範囲で1~48時間かけて溶解させ、ポリイミド溶液にすることができる。 In particular, when continuous coating is performed for a long time, if the solvent in the polyimide solution absorbs moisture in the air and the polyimide may be deposited, a low solvent such as triethylene glycol dimethyl ether, γ-butyrolactone, or cyclopentanone may be used. It is preferable to use a hygroscopic solvent. Also, amide solvents such as N, N-dimethylformamide, N, N-dimethylacetamide, N-methyl-2-pyrrolidone and the like, which are hygroscopic solvents, can be combined with the above low hygroscopic solvent to suppress the precipitation of polyimide. You can also. The polyimide powder can be dissolved in air or in an inert gas at a temperature ranging from room temperature to the boiling point of the solvent over 1 to 48 hours to form a polyimide solution.
本発明の式(2)で表されるポリイミドの固有粘度は、ポリイミドフィルムの膜靭性を考慮すると、0.1dL/g以上、より好ましくは0.2dL/g以上であることが好ましい。固有粘度が0.1dL/g未満だとポリイミドフィルムの膜靭性が確保できず、脆弱なフィルムになる場合がある。 The intrinsic viscosity of the polyimide represented by the formula (2) of the present invention is preferably 0.1 dL / g or more, more preferably 0.2 dL / g or more in consideration of the film toughness of the polyimide film. If the intrinsic viscosity is less than 0.1 dL / g, the toughness of the polyimide film cannot be ensured, and the film may be brittle.
本発明のポリイミドの分子量はその成形性や取扱性の点から重量平均分子量で5000以上であることが好ましく、10000以上であることがより好ましい。なお、ポリイミドの分子量はポリイミド溶液の粘度を目安にすることができる。 The molecular weight of the polyimide of the present invention is preferably 5000 or more, more preferably 10,000 or more in terms of weight average molecular weight from the viewpoints of moldability and handleability. The molecular weight of the polyimide can be based on the viscosity of the polyimide solution.
次に、本発明の上記式(2)で表されるポリイミドを含むポリイミド溶液及びそれを成形して得られるポリイミドフィルムの製造方法について説明する。ポリイミド溶液中のポリイミドの固形分濃度としては、該溶液の用途に応じて適宜選択することができるが、例えばフィルムとする場合、ポリイミドの分子量、製造方法や所望するフィルムの厚さにもよるが、固形分濃度を5重量%以上、好ましくは5重量%~40重量%とすることが好ましい。固形分濃度が低すぎると、十分な膜厚のフィルムを形成することが困難となる場合があり、逆に固形分濃度が高いと溶液粘度が高すぎて塗工が困難となる場合がある。なお、本発明におけるポリイミドの固形分濃度とはポリイミド溶液から定法により溶媒を除去した後に残った固形分(主に上記式(2)で表されるポリイミド)の含量のことを表す。 Next, a polyimide solution containing a polyimide represented by the above formula (2) of the present invention and a method for producing a polyimide film obtained by molding the polyimide solution will be described. The polyimide solid content concentration in the polyimide solution can be appropriately selected according to the use of the solution. For example, in the case of a film, it depends on the molecular weight of the polyimide, the production method, and the desired film thickness. The solid concentration is preferably 5% by weight or more, preferably 5% by weight to 40% by weight. If the solid content concentration is too low, it may be difficult to form a film having a sufficient film thickness. Conversely, if the solid content concentration is high, the solution viscosity may be too high and coating may be difficult. In addition, the solid content concentration of the polyimide in this invention represents the content of the solid content (mainly polyimide represented by the said Formula (2)) remaining after removing a solvent from a polyimide solution by a usual method.
また、本発明の上記式(2)で表されるポリイミドを含むポリイミド溶液には、必要に応じて離型剤、フィラー、シランカップリング剤、架橋剤、末端封止剤、酸化防止剤、消泡剤、レベリング剤などの添加物を加えることができる。 In addition, the polyimide solution containing the polyimide represented by the above formula (2) of the present invention may include a release agent, a filler, a silane coupling agent, a crosslinking agent, a terminal sealing agent, an antioxidant, Additives such as foaming agents and leveling agents can be added.
前記ポリイミド溶液を用いてフィルムを製造する形態について説明するが、膜靭性のある自立膜が作製できれば特に製造方法は限定されない。 Although the form which manufactures a film using the said polyimide solution is demonstrated, a manufacturing method will not be specifically limited if a self-supporting film | membrane with film | membrane toughness can be produced.
具体的には、例えば、ガラス基板などの支持体上にポリイミド溶液を公知の方法、例えば、ドクターブレードなどを用いて塗布後、乾燥し、ポリイミドフィルムを作製する方法がある。または、銅箔等の金属箔上に公知の方法、例えば、ドクターブレードなどを用いて塗布後、乾燥し、ポリイミド/金属箔の積層フィルムを得ることができ、半田実装時の高温工程にも耐えられるフレキシブルプリント配線基板用の銅張積層板にも使用できる。更に前記ポリイミド溶液を半導体やフレキシブル配線基板用の絶縁材料に適用する場合であれば、直接デバイス上にコーティングし、溶媒を乾燥させることで絶縁層が容易に形成できる。 Specifically, for example, there is a known method of applying a polyimide solution on a support such as a glass substrate using a doctor blade or the like and then drying to prepare a polyimide film. Alternatively, it can be applied onto a metal foil such as copper foil using a known method, for example, a doctor blade, and then dried to obtain a polyimide / metal foil laminated film, which can withstand high temperature processes during solder mounting. It can also be used for copper-clad laminates for flexible printed wiring boards. Furthermore, if the polyimide solution is applied to an insulating material for a semiconductor or a flexible wiring board, the insulating layer can be easily formed by coating directly on the device and drying the solvent.
上述のように製造されたポリイミドフィルムは通常、そのガラス転移温度が260℃以上、特に290℃以上となるため特に耐熱性フィルムとして好適に用いられる、例えば、半導体やフレキシブル配線基板用の絶縁材料として用いる場合、その絶縁層のガラス転移温度が260℃以上となるため、無鉛半田実装温度である260℃にも十分に耐え得るので、絶縁材料として好適に使用される。 The polyimide film produced as described above usually has a glass transition temperature of 260 ° C. or higher, particularly 290 ° C. or higher, so that it is particularly suitably used as a heat resistant film. For example, as an insulating material for semiconductors and flexible wiring boards When used, since the glass transition temperature of the insulating layer is 260 ° C. or higher, it can sufficiently withstand 260 ° C., which is a lead-free solder mounting temperature, and is therefore preferably used as an insulating material.
<ポリイミド共重合体>
本発明のポリイミド共重合体(以下、本発明のポリイミドと称することもある)は、下記式(5)で表される繰り返し単位及び下記一般式(6)で表される繰り返し単位を有する。なお、式(6)中、Yは下記式(7)~(12)からなる群より選ばれる少なくとも1種の4価の芳香族基を表す。
<Polyimide copolymer>
The polyimide copolymer of the present invention (hereinafter sometimes referred to as the polyimide of the present invention) has a repeating unit represented by the following formula (5) and a repeating unit represented by the following general formula (6). In the formula (6), Y represents at least one tetravalent aromatic group selected from the group consisting of the following formulas (7) to (12).
本発明にかかるポリイミドの特性を著しく損なわない範囲で、上記式(20)で表されるジアミンとともに他のジアミンが併用可能である。使用可能なジアミンとして例えば、p-フェニレンジアミン、m-フェニレンジアミン、4,4’-ビス(4-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)スルホン、ビス(4-(4-アミノフェノキシ)フェニル)スルホン、2,2-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)ヘキサフルオロプロパン、2,2-ビス(4-アミノフェニル)ヘキサフルオロプロパン、p-ターフェニレンジアミン、ベンジジン、3,3’-ジヒドロキシベンジジン、3,3’-ジメトキシベンジジン、o-トリジン、m-トリジン、1,4-ビス(4-アミノフェノキシ)ベンゼン、1,3-ビス(4-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、4,4’-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、3,3’-ジアミノジフェニルエーテル、2,4’-ジアミノジフェニルエーテル、4,4’-ジアミノジフェニルスルホン、3,3’-ジアミノジフェニルスルホン、4,4’-ジアミノベンゾフェノン、3,3’-ジアミノベンゾフェノン、4,4’-ジアミノベンズアニリド、4-アミノフェニル-4’-アミノベンゾエート、2,4-ジアミノトルエン、2,5-ジアミノトルエン、2,4-ジアミノキシレン、2,4-ジアミノデュレン、4,4’-ジアミノジフェニルメタン、4,4’-メチレンビス(2-メチルアニリン)、4,4’-メチレンビス(2-エチルアニリン)、4,4’-メチレンビス(2,6-ジメチルアニリン)、4,4’-メチレンビス(2,6-ジエチルアニリン)等の芳香族ジアミン、4,4’-メチレンビス(シクロヘキシルアミン)、イソホロンジアミン、トランス-1,4-ジアミノシクロヘキサン、シス-1,4-ジアミノシクロヘキサン、1,4-シクロヘキサンビス(メチルアミン)、2,5-ビス(アミノメチル)ビシクロ〔2.2.1〕ヘプタン、2,6-ビス(アミノメチル)ビシクロ〔2.2.1〕ヘプタン、3,8-ビス(アミノメチル)トリシクロ〔5.2.1.0〕デカン、1,3-ジアミノアダマンタン、2,2-ビス(4-アミノシクロヘキシル)プロパン、2,2-ビス(4-アミノシクロヘキシル)ヘキサフルオロプロパン等の脂環式ジアミン、1,3-プロパンジアミン、1,4-テトラメチレンジアミン、1,5-ペンタメチレンジアミン、1,6-ヘキサメチレンジアミン、1,7-ヘプタメチレンジアミン、1,8-オクタメチレンジアミン、1,9-ノナメチレンジアミン、ジアミノシロキサン等の鎖状脂肪族ジアミンが挙げられる。また、これらを2種類以上併用することもできる。 Other diamines can be used in combination with the diamine represented by the above formula (20) as long as the properties of the polyimide according to the present invention are not significantly impaired. Usable diamines include, for example, p-phenylenediamine, m-phenylenediamine, 4,4′-bis (4-aminophenoxy) biphenyl, bis (4- (3-aminophenoxy) phenyl) sulfone, bis (4- ( 4-aminophenoxy) phenyl) sulfone, 2,2-bis (4- (4-aminophenoxy) phenyl) propane, 2,2-bis (4- (4-aminophenoxy) phenyl) hexafluoropropane, 2,2 -Bis (4-aminophenyl) hexafluoropropane, p-terphenylenediamine, benzidine, 3,3'-dihydroxybenzidine, 3,3'-dimethoxybenzidine, o-tolidine, m-tolidine, 1,4-bis ( 4-aminophenoxy) benzene, 1,3-bis (4-aminophenoxy) benzene, 1,3- (3-aminophenoxy) benzene, 4,4′-diaminodiphenyl ether, 3,4′-diaminodiphenyl ether, 3,3′-diaminodiphenyl ether, 2,4′-diaminodiphenyl ether, 4,4′-diaminodiphenyl sulfone, 3,3′-diaminodiphenylsulfone, 4,4′-diaminobenzophenone, 3,3′-diaminobenzophenone, 4,4′-diaminobenzanilide, 4-aminophenyl-4′-aminobenzoate, 2,4-diamino Toluene, 2,5-diaminotoluene, 2,4-diaminoxylene, 2,4-diaminodurene, 4,4'-diaminodiphenylmethane, 4,4'-methylenebis (2-methylaniline), 4,4'-methylenebis (2-ethylaniline), 4,4'-methylenebis (2,6-dimethylaniline), aromatic diamines such as 4,4′-methylenebis (2,6-diethylaniline), 4,4′-methylenebis (cyclohexylamine), isophoronediamine, trans-1,4-diamino Cyclohexane, cis-1,4-diaminocyclohexane, 1,4-cyclohexanebis (methylamine), 2,5-bis (aminomethyl) bicyclo [2.2.1] heptane, 2,6-bis (aminomethyl) Bicyclo [2.2.1] heptane, 3,8-bis (aminomethyl) tricyclo [5.2.1.0] decane, 1,3-diaminoadamantane, 2,2-bis (4-aminocyclohexyl) propane Alicyclic diamines such as 2,2-bis (4-aminocyclohexyl) hexafluoropropane, 1,3-propanediamine, 1, Chains such as tetramethylenediamine, 1,5-pentamethylenediamine, 1,6-hexamethylenediamine, 1,7-heptamethylenediamine, 1,8-octamethylenediamine, 1,9-nonamethylenediamine, diaminosiloxane And an aliphatic diamine. Two or more of these may be used in combination.
本発明にかかるポリイミド共重合体の特性を著しく損なわない範囲で、上記式(13)~(19)で表されるテトラカルボン酸二無水物とともに、他のテトラカルボン酸二無水物が併用可能である。使用可能なテトラカルボン酸二無水物として例えば、2,3,3’,4’-ビフェニルテトラカルボン酸二無水物、2,3,2’,3’-ビフェニルテトラカルボン酸二無水物、1,4,5,8-ナフタレンテトラカルボン酸二無水物、3,4,3’,4’-ベンゾフェノンテトラカルボン酸二無水物、2,3,3’,4’-ベンゾフェノンテトラカルボン酸二無水物、2,3,2’,3’-ベンゾフェノンテトラカルボン酸二無水物、3,4,3’,4’-ビフェニルエーテルテトラカルボン酸二無水物、3,4,2’,3’-ビフェニルエーテルテトラカルボン酸二無水物、2,3,2’,3’-ビフェニルエーテルテトラカルボン酸二無水物、3,4,3’,4’-ビフェニルスルホンテトラカルボン酸二無水物、3,4,2’,3’-ビフェニルスルホンテトラカルボン酸二無水物、2,3,2’,3’-ビフェニルスルホンテトラカルボン酸二無水物、2,2’-ビス(3,4-ジカルボキシフェニル)ヘキサフルオロプロパン酸二無水物、2,2’-ビス(3,4-ジカルボキシフェニル)プロパン酸二無水物等の芳香族テトラカルボン酸二無水物や、ビシクロ[2.2.2]オクト-7-エン-2,3,5,6-テトラカルボン酸二無水物、5-(ジオキソテトラヒドロフリル-3-メチル-3-シクロヘキセン-1,2-ジカルボン酸無水物、4-(2,5-ジオキソテトラヒドロフラン-3-イル)テトラリン-1,2-ジカルボン酸無水物、テトラヒドロフラン-2,3,4,5-テトラカルボン酸二無水物、ビシクロ-3,3’,4,4’-テトラカルボン酸二無水物、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-シクロペンタンテトラカルボン酸二無水物等の脂肪族テトラカルボン酸二無水物が挙げられる。また、これらを2種類以上併用することもできる。 As long as the characteristics of the polyimide copolymer according to the present invention are not significantly impaired, other tetracarboxylic dianhydrides can be used in combination with the tetracarboxylic dianhydrides represented by the above formulas (13) to (19). is there. Examples of tetracarboxylic dianhydrides that can be used include 2,3,3 ′, 4′-biphenyltetracarboxylic dianhydride, 2,3,2 ′, 3′-biphenyltetracarboxylic dianhydride, 1, 4,5,8-naphthalene tetracarboxylic dianhydride, 3,4,3 ′, 4′-benzophenone tetracarboxylic dianhydride, 2,3,3 ′, 4′-benzophenone tetracarboxylic dianhydride, 2,3,2 ′, 3′-benzophenone tetracarboxylic dianhydride, 3,4,3 ′, 4′-biphenyl ether tetracarboxylic dianhydride, 3,4,2 ′, 3′-biphenyl ether tetra Carboxylic dianhydride, 2,3,2 ′, 3′-biphenyl ether tetracarboxylic dianhydride, 3,4,3 ′, 4′-biphenylsulfone tetracarboxylic dianhydride, 3,4,2 ′ , 3 ' Biphenylsulfonetetracarboxylic dianhydride, 2,3,2 ′, 3′-biphenylsulfonetetracarboxylic dianhydride, 2,2′-bis (3,4-dicarboxyphenyl) hexafluoropropanoic acid dianhydride Aromatic tetracarboxylic dianhydrides such as 2,2′-bis (3,4-dicarboxyphenyl) propanoic dianhydride, and bicyclo [2.2.2] oct-7-ene-2,3 , 5,6-tetracarboxylic dianhydride, 5- (dioxotetrahydrofuryl-3-methyl-3-cyclohexene-1,2-dicarboxylic anhydride, 4- (2,5-dioxotetrahydrofuran-3- Yl) tetralin-1,2-dicarboxylic anhydride, tetrahydrofuran-2,3,4,5-tetracarboxylic dianhydride, bicyclo-3,3 ', 4,4'-tetracarboxylic Aliphatic tetracarboxylic dianhydrides such as dianhydrides, 1,2,3,4-cyclobutanetetracarboxylic dianhydrides, 1,2,3,4-cyclopentanetetracarboxylic dianhydrides, and the like. Two or more of these may be used in combination.
本発明にかかるポリイミド共重合体またはポリアミド酸を合成する際の溶媒としては、本発明にかかるポリイミドに関して上述した溶媒を使用できる。 As the solvent for synthesizing the polyimide copolymer or polyamic acid according to the present invention, the solvents described above with respect to the polyimide according to the present invention can be used.
本発明に使用される上記式(13)~(19)で表されるテトラカルボン酸二無水物の製造方法は特に限定されない。例えば、その構造にエステル基を有する上記式(13)、および上記式(17)~(19)で表されるテトラカルボン酸二無水物は、公知のエステル化反応を適宜用いることにより製造される。具体的には、無水トリメリット酸クロリドを脱水非プロトン性溶媒に溶解させた溶液、及び下記式(21)~(24)のジオールと脱酸剤を脱水非プロトン性溶媒に溶解させた溶液をそれぞれ調製した後、これらの溶液をメカニカルスターラー等を用いて、温度-78℃~0℃の範囲、好ましくは-30℃~-5℃で0.5~48時間、好ましくは1~24時間で徐々に混合させる。その後、反応溶液を0~100℃、好ましくは10~50℃まで昇温させ0.5~24時間、好ましくは1~12時間撹拌しエステル化を完結させた後、生成物を含む溶液から生成物を単離し、適宜洗浄し、真空乾燥器等で100~220℃、より好ましくは120~200℃で乾燥させることで、本発明に使用される上記式(13)、および上記式(17)~(19)で表されるテトラカルボン酸二無水物を得ることができる。本発明の上記式(13)、および上記式(17)~(19)で表されるテトラカルボン酸二無水物の純度が低い場合は、公知の方法、例えば昇華法や再結晶法で適宜精製できる。 The method for producing the tetracarboxylic dianhydride represented by the above formulas (13) to (19) used in the present invention is not particularly limited. For example, the above formula (13) having an ester group in its structure and the tetracarboxylic dianhydride represented by the above formulas (17) to (19) are produced by appropriately using a known esterification reaction. . Specifically, a solution in which trimellitic anhydride chloride is dissolved in a dehydrated aprotic solvent, and a solution in which a diol of the following formulas (21) to (24) and a deoxidizer are dissolved in a dehydrated aprotic solvent are used. After each preparation, these solutions are used in a temperature range of −78 ° C. to 0 ° C., preferably at −30 ° C. to −5 ° C. for 0.5 to 48 hours, preferably 1 to 24 hours using a mechanical stirrer or the like. Mix slowly. Thereafter, the reaction solution is heated to 0 to 100 ° C., preferably 10 to 50 ° C., and stirred for 0.5 to 24 hours, preferably 1 to 12 hours to complete esterification, and then formed from a solution containing the product. The product is isolated, washed as appropriate, and dried at 100 to 220 ° C., more preferably 120 to 200 ° C. with a vacuum dryer or the like, so that the formula (13) and the formula (17) used in the present invention are used. A tetracarboxylic dianhydride represented by (19) can be obtained. When the purity of the tetracarboxylic dianhydride represented by the above formula (13) and the above formulas (17) to (19) of the present invention is low, it is appropriately purified by a known method such as a sublimation method or a recrystallization method. it can.
具体的には、例えば、以下の一段階合成法で合成できる。上記式(20)で表されるジアミンを高沸点溶媒に溶解させ、この溶液に上記式(13)で表されるテトラカルボン酸二無水物と上記式(14)~(19)からなる群より選ばれる少なくとも1種のテトラカルボン酸二無水物の全テトラカルボン酸二無水物量がジアミンと等モルとなるように粉末を徐々に、または分割して加えた後、トルエンなどの共沸剤を加え、不活性ガスを導入しながら150~220℃、より好ましくは、160~190℃でメカニカルスターラー等を用いて0.5~10時間、より好ましくは1~5時間で撹拌し、イミド化時に生成する水を共沸剤とともに系外に除去することでイミド化でき、室温に戻すだけで本発明のポリイミド共重合体を含むポリイミド溶液を得ることができる。尚、イミド化反応の副生成物である水や共沸剤を除去する際に、反応容器内を減圧にすることも可能であり、この工程により固形分濃度を高めることもできる。この時に使用される溶媒は、ポリイミド共重合体が析出しない溶媒であれば特に限定されない。 Specifically, for example, it can be synthesized by the following one-step synthesis method. A diamine represented by the above formula (20) is dissolved in a high boiling point solvent, and a tetracarboxylic dianhydride represented by the above formula (13) and the group consisting of the above formulas (14) to (19) are dissolved in this solution. After adding powder gradually or divided so that the total tetracarboxylic dianhydride amount of at least one selected tetracarboxylic dianhydride is equimolar with diamine, an azeotropic agent such as toluene is added. The mixture is stirred at 150 to 220 ° C., more preferably 160 to 190 ° C. with a mechanical stirrer for 0.5 to 10 hours, more preferably 1 to 5 hours while introducing an inert gas. It can be imidized by removing water to be removed from the system together with the azeotropic agent, and a polyimide solution containing the polyimide copolymer of the present invention can be obtained simply by returning to room temperature. In addition, when removing the water and the azeotropic agent which are by-products of the imidation reaction, the inside of the reaction vessel can be reduced in pressure, and the solid content concentration can be increased by this step. The solvent used at this time is not particularly limited as long as the polyimide copolymer is not precipitated.
また、本発明のポリイミド共重合体及び該ポリイミド共重合体を含む溶液は以下の二段階合成法を用いても合成できる。まず、第一段階目として、上記式(20)で表されるジアミンを溶媒に溶解させ、この溶液に上記式(13)で表されるテトラカルボン酸二無水物と上記式(14)~(19)からなる群より選ばれる少なくとも1種のテトラカルボン酸二無水物の全テトラカルボン酸二無水物量がジアミンと等モルとなるように粉末を徐々に、または分割して加えた後、メカニカルスターラー等を用いて、温度0~100℃の範囲、より好ましくは、5~50℃で0.5~168時間、より好ましくは1~96時間撹拌することで、ポリイミド前駆体であるポリアミド酸が得られる。この際の固形分濃度は、ポリアミド酸の分子量を最大限に高めるため、溶液が均一となり撹拌できる最大濃度が望ましい。即ち、固形分濃度は1~50重量%、より好ましくは5~40重量%である。このような固形分濃度であれば、生成するポリアミド酸の重合度が十分高くなる。また、脂肪族ジアミンを使用した場合、重合初期にしばしば塩形成が起こり、重合が妨害されるが、塩形成を抑制しつつできるだけ重合度を上げるためには、重合時の固形分濃度を上記の好適な濃度範囲に管理することが好ましい。 Further, the polyimide copolymer of the present invention and the solution containing the polyimide copolymer can also be synthesized using the following two-step synthesis method. First, as a first step, a diamine represented by the above formula (20) is dissolved in a solvent, and a tetracarboxylic dianhydride represented by the above formula (13) and the above formulas (14) to ( 19) After adding the powder gradually or divided so that the total amount of tetracarboxylic dianhydride of at least one tetracarboxylic dianhydride selected from the group consisting of 19) is equimolar with diamine, mechanical stirrer The polyamic acid as the polyimide precursor is obtained by stirring at a temperature in the range of 0 to 100 ° C., more preferably 5 to 50 ° C. for 0.5 to 168 hours, more preferably 1 to 96 hours. It is done. In this case, the solid concentration is preferably the maximum concentration at which the solution becomes uniform and can be stirred in order to maximize the molecular weight of the polyamic acid. That is, the solid content concentration is 1 to 50% by weight, more preferably 5 to 40% by weight. With such a solid content concentration, the degree of polymerization of the produced polyamic acid is sufficiently high. In addition, when an aliphatic diamine is used, salt formation often occurs at the initial stage of polymerization and the polymerization is hindered, but in order to increase the degree of polymerization as much as possible while suppressing salt formation, the solid content concentration during the polymerization is It is preferable to manage within a suitable concentration range.
第二段階目として前記で得られたポリイミド前駆体、即ちポリアミド酸をイミド化する方法については、本発明にかかるポリイミドに関して上述した通りである。 As the second step, the polyimide precursor obtained above, that is, the method of imidizing the polyamic acid is as described above for the polyimide according to the present invention.
このようにして得られたポリイミド共重合体粉末は、本発明のポリイミド共重合体を含むポリイミド溶液とするために、溶媒に溶解する必要がある。使用可能な溶媒としては、本発明にかかるポリイミドに関して上述した溶媒が挙げられる。これらを2種類以上混合して用いてもよい。 The polyimide copolymer powder thus obtained needs to be dissolved in a solvent in order to obtain a polyimide solution containing the polyimide copolymer of the present invention. Usable solvents include those described above with respect to the polyimide according to the present invention. Two or more of these may be mixed and used.
特に、長時間にわたり連続塗工する場合、ポリイミド溶液中の溶媒が大気中の水分を吸湿し、ポリイミド共重合体が析出する恐れがある場合に関しても、本発明にかかるポリイミドに関して上述した通りである。 In particular, in the case of continuous coating over a long period of time, the solvent in the polyimide solution absorbs moisture in the air and the polyimide copolymer may be precipitated, as described above for the polyimide according to the present invention. .
本発明のポリイミド共重合体における上記式(5)で表される繰り返し単位と上記式(6)で表される繰り返し単位の含有率は通常1~99mol%であり、低線熱膨張性を保持させる点から、好ましくは2~70mol%とする。 The content of the repeating unit represented by the above formula (5) and the repeating unit represented by the above formula (6) in the polyimide copolymer of the present invention is usually 1 to 99 mol%, and maintains low linear thermal expansion. Therefore, the content is preferably 2 to 70 mol%.
本発明のポリイミド共重合体の固有粘度は、本発明にかかるポリイミドに関して上述した通りである。なお、本発明における固有粘度とは後述する方法で測定された値を表す。 The intrinsic viscosity of the polyimide copolymer of the present invention is as described above for the polyimide according to the present invention. In addition, the intrinsic viscosity in this invention represents the value measured by the method mentioned later.
本発明のポリイミド共重合体の分子量は、本発明にかかるポリイミドに関して上述した通りである。 The molecular weight of the polyimide copolymer of the present invention is as described above for the polyimide according to the present invention.
次に、本発明のポリイミド共重合体を含むポリイミド溶液及びそれを支持体上に塗布・乾燥して得られるポリイミドフィルムの製造方法について説明する。本発明のポリイミド共重合体を含むポリイミド溶液の固形分濃度としては、該溶液の用途に応じて適宜選択することができる。例えばフィルムとする場合、ポリイミド共重合体の分子量、製造方法や所望するフィルムの厚さにもよるが、固形分濃度を5重量%以上とすることが好ましい。固形分濃度が低すぎると、十分な膜厚のフィルムを形成することが困難となる場合があり、逆に固形分濃度が高いと溶液粘度が高すぎて塗工が困難になる場合がある。なお、本発明におけるポリイミド共重合体の固形分濃度とはポリイミド溶液から定法により溶媒を除去した後に残った固形分(主に上記式(6)で表されるポリイミド)の含量のことを表す。 Next, a polyimide solution containing the polyimide copolymer of the present invention and a method for producing a polyimide film obtained by applying and drying the solution on a support will be described. The solid content concentration of the polyimide solution containing the polyimide copolymer of the present invention can be appropriately selected according to the use of the solution. For example, when it is set as a film, although depending on the molecular weight of the polyimide copolymer, the production method, and the desired film thickness, the solid content concentration is preferably 5% by weight or more. If the solid content concentration is too low, it may be difficult to form a film having a sufficient film thickness. Conversely, if the solid content concentration is high, the solution viscosity may be too high and coating may be difficult. In addition, the solid content concentration of the polyimide copolymer in the present invention represents the content of the solid content (mainly polyimide represented by the above formula (6)) remaining after removing the solvent from the polyimide solution by a conventional method.
また、本発明のポリイミド共重合体を含むポリイミド溶液に加えることができる添加物については、本発明にかかるポリイミドに関して上述した通りである。 The additives that can be added to the polyimide solution containing the polyimide copolymer of the present invention are as described above with respect to the polyimide according to the present invention.
本発明のポリイミド共重合体を含むポリイミド溶液を用いて本発明のポリイミドフィルムを製造する形態については、本発明にかかるポリイミドに関して上述した通りである。 The form of producing the polyimide film of the present invention using the polyimide solution containing the polyimide copolymer of the present invention is as described above for the polyimide according to the present invention.
上述のように製造された本発明のポリイミドフィルムは通常、そのガラス転移温度が260℃以上となるため、例えば無鉛半田実装温度である260℃にも十分に耐え得る半導体やフレキシブル配線基板用の絶縁材料として好適に使用される。 Since the polyimide film of the present invention produced as described above usually has a glass transition temperature of 260 ° C. or higher, for example, insulation for semiconductors and flexible wiring boards that can sufficiently withstand the lead-free solder mounting temperature of 260 ° C. It is suitably used as a material.
本発明のポリイミド共重合体を含むポリイミド溶液を用いて製造した本発明のポリイミドフィルムは高い光透過率及び低線熱膨張という特徴、即ち、通常、波長400nmにおける光透過率が30%以上となり、また、線熱膨張係数が40ppm/K以下となるため、透明性及び熱寸法安定性に優れることから各種光学用途や光学デバイスに好適に用いることができる。 The polyimide film of the present invention produced using the polyimide solution containing the polyimide copolymer of the present invention is characterized by high light transmittance and low linear thermal expansion, that is, usually the light transmittance at a wavelength of 400 nm is 30% or more, Moreover, since the linear thermal expansion coefficient is 40 ppm / K or less, it is excellent in transparency and thermal dimensional stability, so that it can be suitably used for various optical applications and optical devices.
本発明を以下のように表現することもできる。 The present invention can also be expressed as follows.
〔4〕
上記式(5)で表される繰り返し単位の含有率が、ポリイミド共重合体中の全繰り返し単位に対し2~70mol%の範囲である〔3〕に記載のポリイミド共重合体。
[4]
The polyimide copolymer according to [3], wherein the content of the repeating unit represented by the formula (5) is in the range of 2 to 70 mol% with respect to all repeating units in the polyimide copolymer.
〔5〕
〔2〕に記載のポリイミド、又は〔3〕若しくは〔4〕に記載のポリイミド共重合体を固形分濃度で5重量%以上含むポリイミド溶液。
[5]
A polyimide solution comprising the polyimide according to [2] or the polyimide copolymer according to [3] or [4] in a solid content concentration of 5% by weight or more.
〔6〕
〔2〕に記載のポリイミド、又は〔3〕若しくは〔4〕に記載のポリイミド共重合体を含むポリイミドフィルム。
[6]
A polyimide film comprising the polyimide according to [2], or the polyimide copolymer according to [3] or [4].
〔7〕
ガラス転移温度が260℃以上である、〔2〕に記載のポリイミド、又は〔3〕若しくは〔4〕に記載のポリイミド共重合体を含む耐熱性フィルム。
[7]
The heat resistant film containing the polyimide as described in [2], or the polyimide copolymer as described in [3] or [4] whose glass transition temperature is 260 degreeC or more.
〔8〕
以下の(A)、(B)及び(C)の特徴を有する〔3〕若しくは〔4〕記載のポリイミドフィルム:
(A)波長400nmにおける光透過率が30%以上;
(B)線熱膨張係数が40ppm/K以下;
(C)ガラス転移温度(Tg)が260℃以上。
[8]
[3] or [4] polyimide film having the following characteristics (A), (B) and (C):
(A) The light transmittance at a wavelength of 400 nm is 30% or more;
(B) the coefficient of linear thermal expansion is 40 ppm / K or less;
(C) Glass transition temperature (Tg) is 260 ° C. or higher.
本発明は上述した各実施形態に限定されるものではなく、請求項に示した範囲で種々の変更が可能であり、異なる実施形態にそれぞれ開示された技術的手段を適宜組み合わせて得られる実施形態についても本発明の技術的範囲に含まれる。さらに、各実施形態にそれぞれ開示された技術的手段を組み合わせることにより、新しい技術的特徴を形成することができる。 The present invention is not limited to the above-described embodiments, and various modifications are possible within the scope shown in the claims, and embodiments obtained by appropriately combining technical means disclosed in different embodiments. Is also included in the technical scope of the present invention. Furthermore, a new technical feature can be formed by combining the technical means disclosed in each embodiment.
以下、本発明を実施例により具体的に説明するが、これら実施例に限定されるものではない。なお、以下の例における物性値は、次の方法により測定した。 Hereinafter, the present invention will be specifically described by way of examples, but the present invention is not limited to these examples. The physical property values in the following examples were measured by the following methods.
(評価方法)
<赤外吸収スペクトル>
フーリエ変換赤外分光光度計FT/IR-4100(日本分光社製)を用い、KBr法にてテトラカルボン酸二無水物の赤外線吸収スペクトルを測定した。また、ポリイミドの赤外線吸収スペクトルについては、ポリイミド溶液を調製後、ガラス基板上に流延し、100℃で30分乾燥してガラス基板上から剥離したポリイミド薄膜試料(約5μm厚)を測定した。
(Evaluation methods)
<Infrared absorption spectrum>
Using a Fourier transform infrared spectrophotometer FT / IR-4100 (manufactured by JASCO Corporation), the infrared absorption spectrum of tetracarboxylic dianhydride was measured by the KBr method. Moreover, about the infrared absorption spectrum of polyimide, after preparing the polyimide solution, it casted on the glass substrate, dried for 30 minutes at 100 degreeC, and measured the polyimide thin film sample (about 5 micrometers thickness) peeled from the glass substrate.
<1H-NMRスペクトル>
フーリエ変換核磁気共鳴JNM―ECP400(JEOL製)を用い、重水素化ジメチルスルホキシド中でテトラカルボン酸二無水物および化学イミド化したポリイミド粉末の1H-NMRスペクトルを測定した。標準物質はテトラメチルシランを使用した。
< 1 H-NMR spectrum>
Using Fourier transform nuclear magnetic resonance JNM-ECP400 (manufactured by JEOL), 1 H-NMR spectra of tetracarboxylic dianhydride and chemically imidized polyimide powder in deuterated dimethyl sulfoxide were measured. Tetramethylsilane was used as the standard substance.
<示差走査熱量分析(融点)>
テトラカルボン酸二無水物の融点は、示差走査熱量分析装置DSC3100(ネッチ・ジャパン社)を用いて、窒素雰囲気中、昇温速度5℃/分で測定した。融点が高く融解ピークがシャープであるほど、高純度であることを示す。
<Differential scanning calorimetry (melting point)>
The melting point of tetracarboxylic dianhydride was measured at a heating rate of 5 ° C./min in a nitrogen atmosphere using a differential scanning calorimeter DSC3100 (Netch Japan). The higher the melting point and the sharper the melting peak, the higher the purity.
<固有粘度>
0.5重量%のポリイミド前駆体溶液、または、ポリイミド溶液をオストワルド粘度計を用いて30℃で還元粘度を測定した。この値をもって固有粘度とみなした。
<Intrinsic viscosity>
The reduced viscosity of a 0.5 wt% polyimide precursor solution or polyimide solution was measured at 30 ° C. using an Ostwald viscometer. This value was regarded as the intrinsic viscosity.
<ポリイミド粉末の有機溶媒への溶解性試験>
ポリイミド粉末0.1gに対し、有機溶媒9.9g(固形分濃度1重量%)をサンプル管に入れ、試験管ミキサーを用いて5分間撹拌して溶解状態を目視で確認した。溶媒として、クロロホルム(CF)、アセトン、テトラヒドロフラン(THF)、1,4-ジオキサン(DOX)、酢酸エチル、シクロペンタノン(CPN)、シクロヘキサノン(CHN)、N,N-ジメチルホルムアミド(DMF)、N,N-ジメチルアセトアミド(DMAc)、N-メチル-2-ピロリドン(NMP)、m-クレゾール、ジメチルスルホキシド(DMSO)、γ-ブチロラクトン(GBL)、トリエチレングリコールジメチルエーテル(Tri-GL)を使用した。評価結果は、室温で溶解した場合を++、加熱により溶解し、且つ室温まで放冷後も均一性を保持していた場合を+、膨潤/一部溶解した場合を±、不溶の場合を-と表示した。
<Solubility test of polyimide powder in organic solvent>
To 0.1 g of polyimide powder, 9.9 g of organic solvent (solid content concentration: 1% by weight) was put in a sample tube, stirred for 5 minutes using a test tube mixer, and the dissolved state was visually confirmed. As a solvent, chloroform (CF), acetone, tetrahydrofuran (THF), 1,4-dioxane (DOX), ethyl acetate, cyclopentanone (CPN), cyclohexanone (CHN), N, N-dimethylformamide (DMF), N , N-dimethylacetamide (DMAc), N-methyl-2-pyrrolidone (NMP), m-cresol, dimethyl sulfoxide (DMSO), γ-butyrolactone (GBL), triethylene glycol dimethyl ether (Tri-GL) were used. The evaluation results are ++ when dissolved at room temperature, + when dissolved by heating and maintaining uniformity after being allowed to cool to room temperature, ± when swollen / partially dissolved, and − Is displayed.
<線熱膨張係数:CTE、およびガラス転移温度:Tg>
ポリイミドフィルムのガラス転移温度は、ネッチ・ジャパン社製TMA4000を用いて(サンプルサイズ 幅5mm、長さ15mm)、荷重(静荷重)を膜厚(μm)×0.5gとして、5℃/minで150℃まで一旦昇温(1回目の昇温)させた後、20℃まで冷却し、さらに5℃/minで昇温(2回目の昇温)させて2回目の昇温時のTMA曲線から接線法より求めた。線熱膨張係数は100~200℃の間の平均値として求めた。
<Linear thermal expansion coefficient: CTE and glass transition temperature: Tg>
The glass transition temperature of the polyimide film is 5 ° C / min with TMA4000 manufactured by Netch Japan Co., Ltd. (sample size width 5 mm, length 15 mm) and the load (static load) is film thickness (μm) × 0.5 g. Temporarily raised to 150 ° C (first temperature rise), then cooled to 20 ° C, further raised at 5 ° C / min (second temperature rise), and from the TMA curve at the second temperature rise Obtained from tangent method. The linear thermal expansion coefficient was determined as an average value between 100 and 200 ° C.
<ポリイミド膜の透過率:T400>
紫外-可視分光光度計V-530(日本分光社製)を用い、波長200~800nmにおけるポリイミドフィルムの光透過率(T%)を測定した。400nmの光透過率を透明性の指標として求め、透明性の評価を行った。
<Transmissivity of polyimide membrane: T400 >
Using a UV-visible spectrophotometer V-530 (manufactured by JASCO Corp.), the light transmittance (T%) of the polyimide film at a wavelength of 200 to 800 nm was measured. A light transmittance of 400 nm was obtained as an index of transparency, and the transparency was evaluated.
<黄色度(イエローネスインデックス):YI>
紫外-可視分光光度計V-530(日本分光社製)を用い、波長380~780nmにおけるポリイミドフィルムの光透過率(T%)からVWCT-615型 カラー診断プログラム(日本分光社製)によってJISK77373に準拠して黄色度(YI)算出した。
<Yellowness (Yellowness Index): YI>
Using a UV-visible spectrophotometer V-530 (manufactured by JASCO Corp.), the light transmittance (T%) of the polyimide film at a wavelength of 380 to 780 nm was determined according to JISK77373 by the VWCT-615 color diagnostic program (manufactured by JASCO Corp.). The yellowness (YI) was calculated based on this.
<全光線透過率およびヘイズ>
Haze Meter NDH4000(日本電色工業製)を用い、ポリイミドフィルムのJISK7361に準拠した全光線透過率とJISK7136に準拠したヘイズ(濁度)を求めた。
<Total light transmittance and haze>
Using Haze Meter NDH4000 (manufactured by Nippon Denshoku Industries Co., Ltd.), the total light transmittance of the polyimide film based on JISK7361 and the haze (turbidity) based on JISK7136 were determined.
<合成例1>(テトラカルボン酸二無水物の合成)
比較例としてスピロ構造を含まないテトラカルボン酸二無水物の合成。
<Synthesis Example 1> (Synthesis of tetracarboxylic dianhydride)
Synthesis of tetracarboxylic dianhydride containing no spiro structure as a comparative example.
ナスフラスコに無水トリメリット酸クロリド8.4228g(40.0mmol)を入れ、脱水N,N-ジメチルホルムアミド(DMF)36mLに室温で溶解させ、セプタムシールして溶液Aを調製した(溶質濃度20wt%)。更に別のフラスコ中で4,4’-ビフェノール3.7242g(20.0mmol)を脱水DMF16mLに室温で溶解し(溶質濃度20wt%)、これにピリジン120mmolを加えてセプタムシールし溶液Bを調製した。氷浴中で冷却、撹拌しながら、溶液Aに溶液Bをシリンジにて徐々に滴下し、その後室温で12時間撹拌した。反応終了後、黄色沈澱物を濾別し、DMFおよびイオン交換水で洗浄した。ピリジン塩酸塩の除去は、硝酸銀水溶液を用いて確認した。洗浄した生成物を回収し、180℃で12時間真空乾燥した。得られた生成物は黄色粉末であり、収量は4.8465g、収率は38.5%であった。得られた生成物は、フーリエ変換赤外分光光度計FT/IR-4100(日本分光社製)より、1861cm-1および1782cm-1に酸無水物基C=O伸縮振動、1730cm-1にエステル基C=O伸縮振動を確認した。また、フーリエ変換核磁気共鳴JNM―ECP400(JEOL製)を用いてプロトンNMR測定を行った結果、DMSO-d6,δ,ppm:7.52(d,4H), 7.58(d,4H), 8.51(d,2H),8.6(m,4H), 8.71-8.76(m,4H)と帰属でき、目的物のテトラカルボン酸二無水物であることが確認された。また、示差走査熱量分析装置DSC3100(ネッチ・ジャパン社)によって融点を測定したところ、326℃に鋭い融解ピークを示したことからこの生成物は高純度であることが示唆された。 8.4228 g (40.0 mmol) of trimellitic anhydride chloride was placed in an eggplant flask, dissolved in 36 mL of dehydrated N, N-dimethylformamide (DMF) at room temperature, and sealed with a septum to prepare solution A (solute concentration 20 wt%). ). Further, 3.7242 g (20.0 mmol) of 4,4′-biphenol was dissolved in 16 mL of dehydrated DMF at room temperature in a separate flask (solute concentration 20 wt%), and 120 mmol of pyridine was added thereto, followed by septum sealing to prepare solution B. . While cooling and stirring in an ice bath, solution B was gradually added dropwise to solution A with a syringe, and then stirred at room temperature for 12 hours. After completion of the reaction, the yellow precipitate was filtered off and washed with DMF and ion exchange water. Removal of pyridine hydrochloride was confirmed using an aqueous silver nitrate solution. The washed product was collected and vacuum dried at 180 ° C. for 12 hours. The obtained product was a yellow powder, the yield was 4.8465 g, and the yield was 38.5%. The resulting product, a Fourier transform infrared than spectrophotometer FT / IR-4100 (manufactured by JASCO Corporation), 1861cm -1 and 1782cm -1 to acid anhydride group C = O stretching vibration, ester 1730 cm -1 The group C = O stretching vibration was confirmed. Further, as a result of proton NMR measurement using Fourier transform nuclear magnetic resonance JNM-ECP400 (manufactured by JEOL), DMSO-d 6 , δ, ppm: 7.52 (d, 4H), 7.58 (d, 4H) ), 8.51 (d, 2H), 8.6 (m, 4H), 8.71-8.76 (m, 4H), confirming that it is the target tetracarboxylic dianhydride It was done. Further, when the melting point was measured with a differential scanning calorimeter DSC3100 (Netch Japan Co., Ltd.), a sharp melting peak was observed at 326 ° C., suggesting that this product is of high purity.
<合成例2>(テトラカルボン酸二無水物の合成)
式(18)で表されるテトラカルボン酸二無水物の合成。
<Synthesis Example 2> (Synthesis of tetracarboxylic dianhydride)
Synthesis of tetracarboxylic dianhydride represented by formula (18).
ナスフラスコに無水トリメリット酸クロリド8.4228g(40.0mmol)を入れ、脱水N,N-ジメチルホルムアミド(DMF)36mLに室温で溶解させ、セプタムシールして溶液Aを調製した(溶質濃度20wt%)。更に別のフラスコ中で4,4’-ビフェノール3.7242g(20.0mmol)を脱水DMF16mLに室温で溶解し(溶質濃度20wt%)、これにピリジン120mmolを加えてセプタムシールし溶液Bを調製した。氷浴中で冷却、撹拌しながら、溶液Aに溶液Bをシリンジにて徐々に滴下し、その後室温で12時間撹拌した。反応終了後、黄色沈澱物を濾別し、DMFおよびイオン交換水で洗浄した。ピリジン塩酸塩の除去は、硝酸銀水溶液を用いて確認した。洗浄した生成物を回収し、180℃で12時間真空乾燥した。得られた生成物は黄色粉末であり、収量は4.8465g、収率は38.5%であった。得られた粗生成物は、γ-ブチロラクトン(GBL)で再結晶し精製した。得られた生成物は、フーリエ変換赤外分光光度計FT/IR-4100(日本分光社製)より、1861cm-1および1782cm-1に酸無水物基C=O伸縮振動、1730cm-1にエステル基C=O伸縮振動を確認した。また、フーリエ変換核磁気共鳴JNM―ECP400(JEOL製)を用いてプロトンNMR測定を行った結果、DMSO-d6,δ,ppm:7.52(d,4H), 7.58(d,4H), 8.51(d,2H),8.6(m,4H), 8.71-8.76(m,4H)と帰属でき、目的物のテトラカルボン酸二無水物であることが確認された。また、示差走査熱量分析装置DSC3100(ネッチ・ジャパン社)によって融点を測定したところ、326℃に鋭い融解ピークを示したことからこの生成物は高純度であることが示唆された。 8.4228 g (40.0 mmol) of trimellitic anhydride chloride was placed in an eggplant flask, dissolved in 36 mL of dehydrated N, N-dimethylformamide (DMF) at room temperature, and sealed with a septum to prepare solution A (solute concentration 20 wt%). ). Further, 3.7242 g (20.0 mmol) of 4,4′-biphenol was dissolved in 16 mL of dehydrated DMF at room temperature in a separate flask (solute concentration 20 wt%), and 120 mmol of pyridine was added thereto, followed by septum sealing to prepare solution B. . While cooling and stirring in an ice bath, solution B was gradually added dropwise to solution A with a syringe, and then stirred at room temperature for 12 hours. After completion of the reaction, the yellow precipitate was filtered off and washed with DMF and ion exchange water. Removal of pyridine hydrochloride was confirmed using an aqueous silver nitrate solution. The washed product was collected and vacuum dried at 180 ° C. for 12 hours. The obtained product was a yellow powder, the yield was 4.8465 g, and the yield was 38.5%. The obtained crude product was purified by recrystallization from γ-butyrolactone (GBL). The resulting product, a Fourier transform infrared than spectrophotometer FT / IR-4100 (manufactured by JASCO Corporation), 1861cm -1 and 1782cm -1 to acid anhydride group C = O stretching vibration, ester 1730 cm -1 The group C = O stretching vibration was confirmed. Further, as a result of proton NMR measurement using Fourier transform nuclear magnetic resonance JNM-ECP400 (manufactured by JEOL), DMSO-d 6 , δ, ppm: 7.52 (d, 4H), 7.58 (d, 4H) ), 8.51 (d, 2H), 8.6 (m, 4H), 8.71-8.76 (m, 4H), confirming that it is the target tetracarboxylic dianhydride It was done. Further, when the melting point was measured with a differential scanning calorimeter DSC3100 (Netch Japan Co., Ltd.), a sharp melting peak was observed at 326 ° C., suggesting that this product is of high purity.
<合成例3>(テトラカルボン酸二無水物の合成)
式(19)で表されるテトラカルボン酸二無水物の合成。
<Synthesis Example 3> (Synthesis of tetracarboxylic dianhydride)
Synthesis of tetracarboxylic dianhydride represented by formula (19).
ナスフラスコに無水トリメリット酸クロリド4.3185(20mmol)を入れ、脱水THF11mLに室温で溶解させ、セプタムシールして溶液Aを調製した(溶質濃度30wt%)。更に別のフラスコ中で2,6-ジヒドロキシナフタレン1.6019g(10.0mmol)を脱水THF4.2mLに室温で溶解し(溶質濃度30wt%)、これにピリジン60mmolを加えてセプタムシールし溶液Bを調製した。氷浴中で冷却、撹拌しながら、溶液Aに溶液Bをシリンジにて徐々に滴下し、その後室温で12時間撹拌した。反応終了後、淡黄色沈澱物を濾別し、THFおよびイオン交換水で洗浄した。ピリジン塩酸塩の除去は、硝酸銀水溶液を用いて確認した。洗浄した生成物を回収し、160℃で12時間真空乾燥した。得られた生成物は黄色粉末であり、収量は4.4853g、収率は88.2%であった。得られた粗生成物は、γ-ブチロラクトン(GBL)で再結晶し精製した。得られた生成物は、フーリエ変換赤外分光光度計FT/IR-4100(日本分光社製)より、1857cm-1および1780cm-1に酸無水物基C=O伸縮振動、1732cm-1にエステル基C=O伸縮振動を確認した。目的物のテトラカルボン酸二無水物であることが確認された。また、示差走査熱量分析装置DSC3100(ネッチ・ジャパン社)によって融点を測定したところ、301℃に鋭い融解ピークを示したことからこの生成物は高純度であることが示唆された。 Trimellitic chloride 4.3185 (20 mmol) was placed in an eggplant flask, dissolved in 11 mL of dehydrated THF at room temperature, and sealed with a septum to prepare solution A (solute concentration 30 wt%). Further, 1.6019 g (10.0 mmol) of 2,6-dihydroxynaphthalene was dissolved in 4.2 mL of dehydrated THF at room temperature in a separate flask (solute concentration 30 wt%). Prepared. While cooling and stirring in an ice bath, solution B was gradually added dropwise to solution A with a syringe, and then stirred at room temperature for 12 hours. After completion of the reaction, the pale yellow precipitate was filtered off and washed with THF and ion exchange water. Removal of pyridine hydrochloride was confirmed using an aqueous silver nitrate solution. The washed product was collected and dried in vacuum at 160 ° C. for 12 hours. The obtained product was a yellow powder, the yield was 4.44853 g, and the yield was 88.2%. The obtained crude product was purified by recrystallization from γ-butyrolactone (GBL). The obtained product was obtained from a Fourier transform infrared spectrophotometer FT / IR-4100 (manufactured by JASCO Corporation) at 1857 cm −1 and 1780 cm −1 with an acid anhydride group C═O stretching vibration and at 1732 cm −1 with an ester. The group C = O stretching vibration was confirmed. It was confirmed that it was the target tetracarboxylic dianhydride. Further, when the melting point was measured with a differential scanning calorimeter DSC3100 (Netch Japan Co., Ltd.), a sharp melting peak was shown at 301 ° C., suggesting that this product is of high purity.
<実施例1>(テトラカルボン酸二無水物の合成)
本発明の式(1)で表されるテトラカルボン酸二無水物の合成。
<Example 1> (Synthesis of tetracarboxylic dianhydride)
Synthesis of tetracarboxylic dianhydride represented by the formula (1) of the present invention.
ナスフラスコに無水トリメリット酸クロリド6.4617g(30.687mmol)を入れ、脱水テトラヒドロフラン(THF)16.6mLに室温で溶解させ、セプタムシールして溶液Aを調製した(溶質濃度30.0重量%)。別のナスフラスコにスピロ[フルオレン-9,9’-(2’,7’-ジヒドロキシキサンテン)]3.6439g(10.057mmol)を脱水THF47.1mLに室温で溶解し(溶質濃度8.0重量%)、これにピリジン4.85mL(60.0mmol)を加えてセプタムシールし溶液Bを調製した。氷浴中で冷却、撹拌しながら、溶液Aに溶液Bをシリンジにて徐々に滴下して1時間撹拌し、その後室温で12時間撹拌した。反応終了後、白色沈澱物を濾別し、THFと水で洗浄した。ピリジン塩酸塩の除去は、洗液に硝酸銀水溶液を添加し白色沈殿が見られなくなったことをもって確認した。洗浄した生成物を回収し、100℃で12時間真空乾燥した。得られた生成物は白色粉末であり、収量は2.8336g、収率は39.8%であった。 6.4617 g (30.687 mmol) of trimellitic anhydride chloride was placed in an eggplant flask, dissolved in 16.6 mL of dehydrated tetrahydrofuran (THF) at room temperature, and sealed with a septum to prepare solution A (solute concentration: 30.0% by weight) ). In a separate eggplant flask, 3.6439 g (10.57 mmol) of spiro [fluorene-9,9 ′-(2 ′, 7′-dihydroxyxanthene)] was dissolved in 47.1 mL of dehydrated THF at room temperature (solute concentration 8.0 wt. %), And 4.85 mL (60.0 mmol) of pyridine was added thereto, followed by septum sealing to prepare Solution B. While cooling and stirring in an ice bath, solution B was gradually added dropwise to solution A with a syringe and stirred for 1 hour, and then stirred at room temperature for 12 hours. After completion of the reaction, the white precipitate was filtered off and washed with THF and water. Removal of pyridine hydrochloride was confirmed by adding a silver nitrate aqueous solution to the washing solution and no white precipitate was observed. The washed product was collected and dried in vacuum at 100 ° C. for 12 hours. The obtained product was a white powder, the yield was 2.8336 g, and the yield was 39.8%.
得られた生成物は、フーリエ変換赤外分光光度計FT/IR-4100(日本分光社製)より、1856cm-1および1781cm-1に酸無水物基C=O伸縮振動吸収帯、1738cm-1にエステル基C=O伸縮振動吸収帯を確認した。また、フーリエ変換核磁気共鳴JNM―ECP400(JEOL製)を用いてプロトンNMR測定を行った結果、DMSO-d6,δ,ppm;8.62-8.51(m,4H),8.27(dd,2H,J=8.0,0.6Hz),8.15(dd,2H,J=8.3,1.8Hz),8.04(d,2H,J=7.7Hz),7.49-7.46(m,4H),7.32(t,2H,J=7.5Hz),6.94(dd,2H,J=8.7,2.4Hz,),6.41(d,2H,J=8.8Hz)と帰属でき、元素分析値は、計算値C:72.47%,H:2.83%,実測値C:72.61%,H:2.97%
と式(1)で表されるテトラカルボン酸二無水物と0.3%以内で一致した。また、示差走査熱量分析装置DSC3100(ネッチ・ジャパン社)によって融点を測定したところ、332℃に鋭い融解ピークを示したことからこの生成物は高純度であることが示唆された。
The obtained product was obtained from Fourier transform infrared spectrophotometer FT / IR-4100 (manufactured by JASCO Corporation) at 1856 cm −1 and 1781 cm −1 at acid anhydride group C═O stretching vibration absorption band, 1738 cm −1. The ester group C = O stretching vibration absorption band was confirmed. As a result of proton NMR measurement using Fourier transform nuclear magnetic resonance JNM-ECP400 (manufactured by JEOL), DMSO-d 6 , δ, ppm; 8.62-8.51 (m, 4H), 8.27 (Dd, 2H, J = 8.0, 0.6 Hz), 8.15 (dd, 2H, J = 8.3, 1.8 Hz), 8.04 (d, 2H, J = 7.7 Hz), 7.49-7.46 (m, 4H), 7.32 (t, 2H, J = 7.5 Hz), 6.94 (dd, 2H, J = 8.7, 2.4 Hz), 6. 41 (d, 2H, J = 8.8 Hz), and the elemental analysis values are calculated C: 72.47%, H: 2.83%, measured C: 72.61%, H: 2. 97%
With the tetracarboxylic dianhydride represented by the formula (1) within 0.3%. Further, when the melting point was measured with a differential scanning calorimeter DSC3100 (Netch Japan Co., Ltd.), a sharp melting peak was observed at 332 ° C., suggesting that this product was of high purity.
<実施例2>(ポリアミド酸の重合;DABA系)
4,4’-ジアミノベンズアニリド(DABA)0.6818g(3mmol)を脱水N,N-ジメチルアセトアミド(DMAc)6.57gに溶解した。ここに実施例1で合成した式(1)で表されるテトラカルボン酸二無水物粉末2.1378g(3mmol)をゆっくり加えて固形分濃度30.0重量%で撹拌した。適宜DMAcで希釈しながら室温で72時間撹拌しポリイミド前駆体であるポリアミド酸を得た(固形分濃度15.0重量%)。得られたポリアミド酸の固有粘度は、1.41dL/gであった。
<Example 2> (Polyamide acid polymerization; DABA system)
0.6818 g (3 mmol) of 4,4′-diaminobenzanilide (DABA) was dissolved in 6.57 g of dehydrated N, N-dimethylacetamide (DMAc). To this, 2.1378 g (3 mmol) of tetracarboxylic dianhydride powder represented by the formula (1) synthesized in Example 1 was slowly added and stirred at a solid content concentration of 30.0% by weight. While appropriately diluted with DMAc, the mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor (solid content concentration: 15.0% by weight). The intrinsic viscosity of the obtained polyamic acid was 1.41 dL / g.
(化学イミド化によるポリイミドの合成)
得られたポリアミド酸溶液を脱水DMAcで固形分濃度8重量%に希釈後、3.0627g(30mmmol)の無水酢酸と1.1865g(15mmol)のピリジンの混合溶液を室温でゆっくり滴下し、その後24時間撹拌した。得られたポリイミド溶液を大量の脱イオン水に加え、目的生成物を沈澱させた。得られた析出物をメタノールで十分洗浄し、100℃で12時間真空乾燥しポリイミド粉末を得た。得られたポリイミドの固有粘度は、0.69dL/gであった。イミド化の完結は、1H-NMRよりポリアミド酸中のカルボキシ基のプロトン消失、及びFT-IRによって確認した(図1)。得られたポリイミド粉末の各溶媒に対する溶解性評価を表1に示す。
(Polyimide synthesis by chemical imidization)
The obtained polyamic acid solution was diluted with dehydrated DMAc to a solid concentration of 8% by weight, and then a mixed solution of 3.0627 g (30 mmol) of acetic anhydride and 1.1865 g (15 mmol) of pyridine was slowly added dropwise at room temperature. Stir for hours. The resulting polyimide solution was added to a large amount of deionized water to precipitate the desired product. The obtained precipitate was sufficiently washed with methanol and vacuum dried at 100 ° C. for 12 hours to obtain a polyimide powder. The intrinsic viscosity of the obtained polyimide was 0.69 dL / g. Completion of imidation was confirmed by proton disappearance of the carboxy group in the polyamic acid and FT-IR by 1 H-NMR (FIG. 1). Table 1 shows the evaluation of the solubility of the obtained polyimide powder in each solvent.
(ポリイミド溶液の調製およびポリイミドフィルムの作製)
得られたポリイミド粉末を室温でDMAcに再溶解し、15重量%の溶液を調製した。このポリイミド溶液をガラス基板上に流延し、60℃で2時間熱風乾燥器によって乾燥した。その後、ガラス基板ごと減圧下200℃で1時間乾燥した後、室温まで放冷後、ガラス基板からポリイミドフィルムを剥した。このポリイミドフィルムをもう一度減圧下で300℃1時間乾燥した。得られたフィルムの膜物性を表2に示す。
(Preparation of polyimide solution and preparation of polyimide film)
The obtained polyimide powder was redissolved in DMAc at room temperature to prepare a 15 wt% solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was again dried under reduced pressure at 300 ° C. for 1 hour. Table 2 shows the film physical properties of the obtained film.
<実施例3>(ポリアミド酸の重合;4,4’‐ODA系)
4,4’-オキシジアニリン(4,4’-ODA)0.6007g(3mmol)を脱水N,N-ジメチルアセトアミド(DMAc)6.39gに溶解した。ここに実施例1で合成した式(1)で表されるテトラカルボン酸二無水物粉末2.1378g(3mmol)をゆっくり加えて固形分濃度30.0重量%で撹拌した。適宜DMAcで希釈しながら室温で72時間撹拌しポリイミド前駆体であるポリアミド酸を得た(固形分濃度22.9重量%)。得られたポリアミド酸の固有粘度は、0.96dL/gであった。
<Example 3> (Polyamide acid polymerization; 4,4'-ODA system)
0.6007 g (3 mmol) of 4,4′-oxydianiline (4,4′-ODA) was dissolved in 6.39 g of dehydrated N, N-dimethylacetamide (DMAc). To this, 2.1378 g (3 mmol) of tetracarboxylic dianhydride powder represented by the formula (1) synthesized in Example 1 was slowly added and stirred at a solid content concentration of 30.0% by weight. While appropriately diluting with DMAc, the mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor (solid content concentration 22.9% by weight). The intrinsic viscosity of the obtained polyamic acid was 0.96 dL / g.
(化学イミド化によるポリイミドの合成)
得られたポリアミド酸溶液を脱水DMAcで固形分濃度8重量%に希釈後、3.0627g(30mmmol)の無水酢酸と1.1865g(15mmol)のピリジンの混合溶液を室温でゆっくり滴下し、その後24時間撹拌した。得られたポリイミド溶液を大量の脱イオン水に加え、目的生成物を沈澱させた。得られた析出物をメタノールで十分洗浄し、100℃で12時間真空乾燥しポリイミド粉末を得た。得られたポリイミドの固有粘度は、1.17dL/gであった。イミド化の完結は、1H-NMRよりポリアミド酸中のアミドプロトン消失、及びFT-IRによって確認した(図2)。得られたポリイミド粉末の各溶媒に対する溶解性評価を表1に示す。
(Polyimide synthesis by chemical imidization)
The obtained polyamic acid solution was diluted with dehydrated DMAc to a solid concentration of 8% by weight, and then a mixed solution of 3.0627 g (30 mmol) of acetic anhydride and 1.1865 g (15 mmol) of pyridine was slowly added dropwise at room temperature. Stir for hours. The resulting polyimide solution was added to a large amount of deionized water to precipitate the desired product. The obtained precipitate was sufficiently washed with methanol and vacuum dried at 100 ° C. for 12 hours to obtain a polyimide powder. The intrinsic viscosity of the obtained polyimide was 1.17 dL / g. Completion of imidation was confirmed by disappearance of amide protons in the polyamic acid and 1 FT-IR by 1 H-NMR (FIG. 2). Table 1 shows the evaluation of the solubility of the obtained polyimide powder in each solvent.
(ポリイミド溶液の調製およびポリイミドフィルムの作製)
得られたポリイミド粉末を室温でN-メチル-2-ピロリドン(NMP)に再溶解し、15重量%の溶液を調製した。このポリイミド溶液をガラス基板上に流延し、80℃で2時間熱風乾燥器によって乾燥した。その後、ガラス基板ごと減圧下200℃で1時間乾燥した後、室温まで放冷後、ガラス基板からポリイミドフィルムを剥した。このポリイミドフィルムをもう一度減圧下で300℃1時間乾燥した。得られたフィルムの膜物性を表2に示す。
(Preparation of polyimide solution and preparation of polyimide film)
The obtained polyimide powder was redissolved in N-methyl-2-pyrrolidone (NMP) at room temperature to prepare a 15% by weight solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 80 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was again dried under reduced pressure at 300 ° C. for 1 hour. Table 2 shows the film physical properties of the obtained film.
<実施例4>(ポリアミド酸の重合;TFMB系)
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)0.9607g(3mmol)を脱水N,N-ジメチルアセトアミド(DMAc)7.2gに溶解した。ここに実施例1で合成した式(1)で表されるテトラカルボン酸二無水物粉末2.1378g(3mmol)をゆっくり加えて固形分濃度30.0重量%で撹拌した。適宜DMAcで希釈しながら室温で72時間撹拌しポリイミド前駆体であるポリアミド酸を得た(固形分濃度23.6重量%)。得られたポリアミド酸の固有粘度は、0.94dL/gであった。
<Example 4> (Polyamide acid polymerization; TFMB system)
0.9607 g (3 mmol) of 4,4′-diamino-2,2′-bis (trifluoromethyl) biphenyl (TFMB) was dissolved in 7.2 g of dehydrated N, N-dimethylacetamide (DMAc). To this, 2.1378 g (3 mmol) of tetracarboxylic dianhydride powder represented by the formula (1) synthesized in Example 1 was slowly added and stirred at a solid content concentration of 30.0% by weight. While appropriately diluted with DMAc, the mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor (solid content concentration 23.6% by weight). The obtained polyamic acid had an intrinsic viscosity of 0.94 dL / g.
(化学イミド化によるポリイミドの合成)
得られたポリアミド酸溶液を脱水DMAcで固形分濃度8重量%に希釈後、3.0627g(30mmmol)の無水酢酸と1.1865g(15mmol)のピリジンの混合溶液を室温でゆっくり滴下し、その後24時間撹拌した。得られたポリイミド溶液を大量の脱イオン水に加え、目的生成物を沈澱させた。得られた析出物をメタノールで十分洗浄し、100℃で12時間真空乾燥しポリイミド粉末を得た。得られたポリイミドの固有粘度は、0.81dL/gであった。イミド化の完結は、1H-NMRよりポリアミド酸中のアミドプロトン消失、及びFT-IRによって確認した(図3)。得られたポリイミド粉末の各溶媒に対する溶解性評価を表1に示す。
(Polyimide synthesis by chemical imidization)
The obtained polyamic acid solution was diluted with dehydrated DMAc to a solid concentration of 8% by weight, and then a mixed solution of 3.0627 g (30 mmol) of acetic anhydride and 1.1865 g (15 mmol) of pyridine was slowly added dropwise at room temperature. Stir for hours. The resulting polyimide solution was added to a large amount of deionized water to precipitate the desired product. The obtained precipitate was sufficiently washed with methanol and vacuum dried at 100 ° C. for 12 hours to obtain a polyimide powder. The intrinsic viscosity of the obtained polyimide was 0.81 dL / g. Completion of imidization was confirmed by disappearance of amide protons in the polyamic acid and FT-IR by 1 H-NMR (FIG. 3). Table 1 shows the evaluation of the solubility of the obtained polyimide powder in each solvent.
(ポリイミド溶液の調製およびポリイミドフィルムの作製)
得られたポリイミド粉末を室温でシクロペンタノン(CPN)に再溶解し、23重量%の溶液を調製した。このポリイミド溶液をガラス基板上に流延し、60℃で2時間熱風乾燥器によって乾燥した。その後、ガラス基板ごと減圧下200℃で1時間乾燥した後、室温まで放冷後、ガラス基板からポリイミドフィルムを剥した。このポリイミドフィルムをもう一度減圧下で280℃1時間乾燥した。得られたフィルムの膜物性を表2に示す。
(Preparation of polyimide solution and preparation of polyimide film)
The obtained polyimide powder was redissolved in cyclopentanone (CPN) at room temperature to prepare a 23 wt% solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was dried again under reduced pressure at 280 ° C. for 1 hour. Table 2 shows the film physical properties of the obtained film.
<実施例5>
(ポリアミド酸の重合)
式(20)で表されるジアミン0.9607g(3mmol)を脱水N,N-ジメチルアセトアミド(DMAc)6.3gに溶解した。ここに式(1)で表されるテトラカルボン酸二無水物粉末1.4965g(2.1mmol)と式(16)で表されるテトラカルボン酸二無水物粉末0.2414g(0.9mmol)とをゆっくり加えて固形分濃度30重量%で撹拌した。適宜DMAcで希釈しながら室温で72時間撹拌しポリイミド前駆体であるポリアミド酸を得た(固形分濃度22.9重量%)。得られたポリアミド酸の固有粘度は、1.52dL/gであった。
<Example 5>
(Polyamide acid polymerization)
0.9607 g (3 mmol) of the diamine represented by the formula (20) was dissolved in 6.3 g of dehydrated N, N-dimethylacetamide (DMAc). Here, 1.4965 g (2.1 mmol) of tetracarboxylic dianhydride powder represented by the formula (1), 0.2414 g (0.9 mmol) of tetracarboxylic dianhydride powder represented by the formula (16), and Was slowly added and stirred at a solid concentration of 30% by weight. While appropriately diluting with DMAc, the mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor (solid content concentration 22.9% by weight). The resulting polyamic acid had an intrinsic viscosity of 1.52 dL / g.
(化学イミド化によるポリイミドの合成)
得られたポリアミド酸溶液を脱水DMAcで固形分濃度8重量%に希釈後、3.0627g(30mmmol)の無水酢酸と1.1865g(15mmol)のピリジンの混合溶液を室温でゆっくり滴下し、その後24時間撹拌した。得られたポリイミド溶液を大量の脱イオン水に加え、目的生成物を沈澱させた。得られた析出物をメタノールで十分洗浄し、100℃で12時間真空乾燥しポリイミド粉末を得た。得られたポリイミドの固有粘度は、0.99dL/gであった。イミド化の完結は、FT-IRによって確認した(図4)。得られたポリイミド粉末の各溶媒に対する溶解性評価を表3に示す。
(Polyimide synthesis by chemical imidization)
The obtained polyamic acid solution was diluted with dehydrated DMAc to a solid concentration of 8% by weight, and then a mixed solution of 3.0627 g (30 mmol) of acetic anhydride and 1.1865 g (15 mmol) of pyridine was slowly added dropwise at room temperature. Stir for hours. The resulting polyimide solution was added to a large amount of deionized water to precipitate the desired product. The obtained precipitate was sufficiently washed with methanol and vacuum dried at 100 ° C. for 12 hours to obtain a polyimide powder. The intrinsic viscosity of the obtained polyimide was 0.99 dL / g. Completion of imidization was confirmed by FT-IR (FIG. 4). Table 3 shows the evaluation of the solubility of the obtained polyimide powder in each solvent.
(ポリイミド溶液の調製およびポリイミドフィルムの作製)
得られたポリイミド粉末を室温でシクロペンタノン(CPN)に再溶解し、12重量%の溶液を調製した。このポリイミド溶液をガラス基板上に流延し、60℃で2時間熱風乾燥器によって乾燥した。その後、ガラス基板ごと減圧下200℃で1時間乾燥した後、室温まで放冷後、ガラス基板からポリイミドフィルムを剥した。このポリイミドフィルムをもう一度減圧下で280℃1時間乾燥した。得られたフィルムの膜物性を表4に示す。
(Preparation of polyimide solution and preparation of polyimide film)
The obtained polyimide powder was redissolved in cyclopentanone (CPN) at room temperature to prepare a 12 wt% solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was dried again under reduced pressure at 280 ° C. for 1 hour. Table 4 shows the film physical properties of the obtained film.
<実施例6>
(ポリアミド酸の重合)
式(20)で表されるジアミン0.9607g(3mmol)を脱水DMAc6.0gに溶解した。ここに式(1)で表されるテトラカルボン酸二無水物粉末1.2827g(1.8mmol)と式(16)で表されるテトラカルボン酸二無水物粉末0.3218g(1.2mmol)とをゆっくり加えて固形分濃度30重量%で撹拌した。適宜DMAcで希釈しながら室温で72時間撹拌しポリイミド前駆体であるポリアミド酸を得た(固形分濃度24.6重量%)。得られたポリアミド酸の固有粘度は、1.15dL/gであった。
<Example 6>
(Polyamide acid polymerization)
0.9607 g (3 mmol) of the diamine represented by the formula (20) was dissolved in 6.0 g of dehydrated DMAc. A tetracarboxylic dianhydride powder represented by the formula (1) (1.2827 g, 1.8 mmol) and a tetracarboxylic dianhydride powder represented by the formula (16) (0.3218 g, 1.2 mmol) Was slowly added and stirred at a solid concentration of 30% by weight. While appropriately diluted with DMAc, the mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor (solid content concentration 24.6% by weight). The obtained polyamic acid had an intrinsic viscosity of 1.15 dL / g.
(化学イミド化によるポリイミドの合成)
得られたポリアミド酸溶液を脱水DMAcで固形分濃度8重量%に希釈後、3.0627g(30mmmol)の無水酢酸と1.1865g(15mmol)のピリジンの混合溶液を室温でゆっくり滴下し、その後24時間撹拌した。得られたポリイミド溶液を大量の脱イオン水に加え、目的生成物を沈澱させた。得られた析出物をメタノールで十分洗浄し、100℃で12時間真空乾燥しポリイミド粉末を得た。得られたポリイミドの固有粘度は、1.10dL/gであった。イミド化の完結は、FT-IRによって確認した(図5)。得られたポリイミド粉末の各溶媒に対する溶解性評価を表3に示す。
(Polyimide synthesis by chemical imidization)
The obtained polyamic acid solution was diluted with dehydrated DMAc to a solid concentration of 8% by weight, and then a mixed solution of 3.0627 g (30 mmol) of acetic anhydride and 1.1865 g (15 mmol) of pyridine was slowly added dropwise at room temperature. Stir for hours. The resulting polyimide solution was added to a large amount of deionized water to precipitate the desired product. The obtained precipitate was sufficiently washed with methanol and vacuum dried at 100 ° C. for 12 hours to obtain a polyimide powder. The intrinsic viscosity of the obtained polyimide was 1.10 dL / g. Completion of imidization was confirmed by FT-IR (FIG. 5). Table 3 shows the evaluation of the solubility of the obtained polyimide powder in each solvent.
(ポリイミド溶液の調製およびポリイミドフィルムの作製)
得られたポリイミド粉末を室温でCPNに再溶解し、6重量%の溶液を調製した。このポリイミド溶液をガラス基板上に流延し、60℃で2時間熱風乾燥器によって乾燥した。その後、ガラス基板ごと減圧下200℃で1時間乾燥した後、室温まで放冷後、ガラス基板からポリイミドフィルムを剥した。このポリイミドフィルムをもう一度減圧下で280℃1時間乾燥した。得られたフィルムの膜物性を表4に示す。
(Preparation of polyimide solution and preparation of polyimide film)
The obtained polyimide powder was redissolved in CPN at room temperature to prepare a 6 wt% solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was dried again under reduced pressure at 280 ° C. for 1 hour. Table 4 shows the film physical properties of the obtained film.
<実施例7>
実施例6で得られたポリイミド粉末を室温でDMAcに再溶解し、10重量%の溶液を調製した。このポリイミド溶液をガラス基板上に流延し、60℃で2時間熱風乾燥器によって乾燥した。その後、ガラス基板ごと減圧下200℃で1時間乾燥した後、室温まで放冷後、ガラス基板からポリイミドフィルムを剥した。このポリイミドフィルムをもう一度減圧下で280℃1時間乾燥した。得られたフィルムの膜物性を表4に示す。
<Example 7>
The polyimide powder obtained in Example 6 was redissolved in DMAc at room temperature to prepare a 10% by weight solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was dried again under reduced pressure at 280 ° C. for 1 hour. Table 4 shows the film physical properties of the obtained film.
<実施例8>
(ポリアミド酸の重合)
式(20)で表されるジアミン0.9607g(3mmol)を脱水DMAc6.9gに溶解した。ここに式(1)で表されるテトラカルボン酸二無水物粉末1.4965g(2.1mmol)と式(18)で表されるテトラカルボン酸二無水物粉末0.4810g(0.9mmol)とをゆっくり加えて固形分濃度30重量%で撹拌した。適宜DMAcで希釈しながら室温で72時間撹拌しポリイミド前駆体であるポリアミド酸を得た(固形分濃度21重量%)。得られたポリアミド酸の固有粘度は、1.36dL/gであった。
<Example 8>
(Polyamide acid polymerization)
0.9607 g (3 mmol) of the diamine represented by the formula (20) was dissolved in 6.9 g of dehydrated DMAc. Here, 1.4965 g (2.1 mmol) of tetracarboxylic dianhydride powder represented by the formula (1), 0.4810 g (0.9 mmol) of tetracarboxylic dianhydride powder represented by the formula (18), and Was slowly added and stirred at a solid concentration of 30% by weight. While appropriately diluted with DMAc, the mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor (solid content concentration 21% by weight). The resulting polyamic acid had an intrinsic viscosity of 1.36 dL / g.
(化学イミド化によるポリイミドの合成)
得られたポリアミド酸溶液を脱水DMAcで固形分濃度8重量%に希釈後、3.0627g(30mmmol)の無水酢酸と1.1865g(15mmol)のピリジンの混合溶液を室温でゆっくり滴下し、その後24時間撹拌した。得られたポリイミド溶液を大量の脱イオン水に加え、目的生成物を沈澱させた。得られた析出物をメタノールで十分洗浄し、100℃で12時間真空乾燥しポリイミド粉末を得た。得られたポリイミドの固有粘度は、0.76dL/gであった。イミド化の完結は、FT-IRによって確認した(図6)。得られたポリイミド粉末の各溶媒に対する溶解性評価を表3に示す。
(Polyimide synthesis by chemical imidization)
The obtained polyamic acid solution was diluted with dehydrated DMAc to a solid concentration of 8% by weight, and then a mixed solution of 3.0627 g (30 mmol) of acetic anhydride and 1.1865 g (15 mmol) of pyridine was slowly added dropwise at room temperature. Stir for hours. The resulting polyimide solution was added to a large amount of deionized water to precipitate the desired product. The obtained precipitate was sufficiently washed with methanol and vacuum dried at 100 ° C. for 12 hours to obtain a polyimide powder. The intrinsic viscosity of the obtained polyimide was 0.76 dL / g. Completion of imidization was confirmed by FT-IR (FIG. 6). Table 3 shows the evaluation of the solubility of the obtained polyimide powder in each solvent.
(ポリイミド溶液の調製およびポリイミドフィルムの作製)
得られたポリイミド粉末を室温でCPNに再溶解し、20重量%の溶液を調製した。このポリイミド溶液をガラス基板上に流延し、60℃で2時間熱風乾燥器によって乾燥した。その後、ガラス基板ごと減圧下200℃で1時間乾燥した後、室温まで放冷後、ガラス基板からポリイミドフィルムを剥した。このポリイミドフィルムをもう一度減圧下で250℃1時間乾燥した。得られたフィルムの膜物性を表4に示す。
(Preparation of polyimide solution and preparation of polyimide film)
The obtained polyimide powder was redissolved in CPN at room temperature to prepare a 20 wt% solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was again dried under reduced pressure at 250 ° C. for 1 hour. Table 4 shows the film physical properties of the obtained film.
<実施例9>
実施例8で得られたポリイミド粉末を室温でDMAcに再溶解し、20重量%の溶液を調製した。このポリイミド溶液をガラス基板上に流延し、60℃で2時間熱風乾燥器によって乾燥した。その後、ガラス基板ごと減圧下200℃で1時間乾燥した後、室温まで放冷後、ガラス基板からポリイミドフィルムを剥した。このポリイミドフィルムをもう一度減圧下で250℃1時間乾燥した。得られたフィルムの膜物性を表4に示す。
<Example 9>
The polyimide powder obtained in Example 8 was redissolved in DMAc at room temperature to prepare a 20% by weight solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was again dried under reduced pressure at 250 ° C. for 1 hour. Table 4 shows the film physical properties of the obtained film.
<実施例10>
(ポリアミド酸の重合)
式(20)で表されるジアミン0.9607g(3mmol)を脱水DMAc6.7gに溶解した。ここに式(1)で表されるテトラカルボン酸二無水物粉末1.2827g(1.8mmol)と式(18)で表されるテトラカルボン酸二無水物粉末0.6413g(1.2mmol)とをゆっくり加えて固形分濃度30重量%で撹拌した。適宜DMAcで希釈しながら室温で72時間撹拌しポリイミド前駆体であるポリアミド酸を得た(固形分濃度25.1重量%)。得られたポリアミド酸の固有粘度は、1.30dL/gであった。
<Example 10>
(Polyamide acid polymerization)
0.9607 g (3 mmol) of the diamine represented by the formula (20) was dissolved in 6.7 g of dehydrated DMAc. Here, 1.28827 g (1.8 mmol) of tetracarboxylic dianhydride powder represented by formula (1) and 0.6413 g (1.2 mmol) of tetracarboxylic dianhydride powder represented by formula (18) Was slowly added and stirred at a solid concentration of 30% by weight. While appropriately diluted with DMAc, the mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor (solid content concentration 25.1% by weight). The obtained polyamic acid had an intrinsic viscosity of 1.30 dL / g.
(化学イミド化によるポリイミドの合成)
得られたポリアミド酸溶液を脱水DMAcで固形分濃度8重量%に希釈後、3.0627g(30mmmol)の無水酢酸と1.1865g(15mmol)のピリジンの混合溶液を室温でゆっくり滴下し、その後24時間撹拌した。得られたポリイミド溶液を大量の脱イオン水に加え、目的生成物を沈澱させた。得られた析出物をメタノールで十分洗浄し、100℃で12時間真空乾燥しポリイミド粉末を得た。得られたポリイミドの固有粘度は、0.87dL/gであった。イミド化の完結は、FT-IRによって確認した(図7)。得られたポリイミド粉末の各溶媒に対する溶解性評価を表3に示す。
(Polyimide synthesis by chemical imidization)
The obtained polyamic acid solution was diluted with dehydrated DMAc to a solid concentration of 8% by weight, and then a mixed solution of 3.0627 g (30 mmol) of acetic anhydride and 1.1865 g (15 mmol) of pyridine was slowly added dropwise at room temperature. Stir for hours. The resulting polyimide solution was added to a large amount of deionized water to precipitate the desired product. The obtained precipitate was sufficiently washed with methanol and vacuum dried at 100 ° C. for 12 hours to obtain a polyimide powder. The intrinsic viscosity of the obtained polyimide was 0.87 dL / g. The completion of imidization was confirmed by FT-IR (FIG. 7). Table 3 shows the evaluation of the solubility of the obtained polyimide powder in each solvent.
(ポリイミド溶液の調製およびポリイミドフィルムの作製)
得られたポリイミド粉末を室温でCPNに再溶解し、20重量%の溶液を調製した。このポリイミド溶液をガラス基板上に流延し、60℃で2時間熱風乾燥器によって乾燥した。その後、ガラス基板ごと減圧下200℃で1時間乾燥した後、室温まで放冷後、ガラス基板からポリイミドフィルムを剥した。このポリイミドフィルムをもう一度減圧下で250℃1時間乾燥した。得られたフィルムの膜物性を表4に示す。
(Preparation of polyimide solution and preparation of polyimide film)
The obtained polyimide powder was redissolved in CPN at room temperature to prepare a 20 wt% solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was again dried under reduced pressure at 250 ° C. for 1 hour. Table 4 shows the film physical properties of the obtained film.
<実施例11>
実施例10で得られたポリイミド粉末を室温でDMAcに再溶解し、20重量%の溶液を調製した。このポリイミド溶液をガラス基板上に流延し、60℃で2時間熱風乾燥器によって乾燥した。その後、ガラス基板ごと減圧下200℃で1時間乾燥した後、室温まで放冷後、ガラス基板からポリイミドフィルムを剥した。このポリイミドフィルムをもう一度減圧下で250℃1時間乾燥した。得られたフィルムの膜物性を表4に示す。
<Example 11>
The polyimide powder obtained in Example 10 was redissolved in DMAc at room temperature to prepare a 20% by weight solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was again dried under reduced pressure at 250 ° C. for 1 hour. Table 4 shows the film physical properties of the obtained film.
<実施例12>
(ポリアミド酸の重合)
式(20)で表されるジアミン0.9607g(3mmol)を脱水DMAc6.6gに溶解した。ここに式(1)で表されるテトラカルボン酸二無水物粉末1.0689g(1.5mmol)と式(18)で表されるテトラカルボン酸二無水物粉末0.8016g(1.5mmol)とをゆっくり加えて固形分濃度30重量%で撹拌した。適宜DMAcで希釈しながら室温で72時間撹拌しポリイミド前駆体であるポリアミド酸を得た(固形分濃度20.7重量%)。得られたポリアミド酸の固有粘度は、1.23dL/gであった。
<Example 12>
(Polyamide acid polymerization)
0.9607 g (3 mmol) of the diamine represented by the formula (20) was dissolved in 6.6 g of dehydrated DMAc. Here, 1.0689 g (1.5 mmol) of tetracarboxylic dianhydride powder represented by formula (1), 0.8016 g (1.5 mmol) of tetracarboxylic dianhydride powder represented by formula (18), and Was slowly added and stirred at a solid concentration of 30% by weight. While appropriately diluted with DMAc, the mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor (solid content concentration: 20.7% by weight). The obtained polyamic acid had an intrinsic viscosity of 1.23 dL / g.
(化学イミド化によるポリイミドの合成)
得られたポリアミド酸溶液を脱水DMAcで固形分濃度8重量%に希釈後、3.0627g(30mmmol)の無水酢酸と1.1865g(15mmol)のピリジンの混合溶液を室温でゆっくり滴下し、その後24時間撹拌した。得られたポリイミド溶液を大量の脱イオン水に加え、目的生成物を沈澱させた。得られた析出物をメタノールで十分洗浄し、100℃で12時間真空乾燥しポリイミド粉末を得た。得られたポリイミドの固有粘度は、0.79dL/gであった。イミド化の完結は、FT-IRによって確認した(図8)。得られたポリイミド粉末の各溶媒に対する溶解性評価を表3に示す。
(Polyimide synthesis by chemical imidization)
The obtained polyamic acid solution was diluted with dehydrated DMAc to a solid concentration of 8% by weight, and then a mixed solution of 3.0627 g (30 mmol) of acetic anhydride and 1.1865 g (15 mmol) of pyridine was slowly added dropwise at room temperature. Stir for hours. The resulting polyimide solution was added to a large amount of deionized water to precipitate the desired product. The obtained precipitate was sufficiently washed with methanol and vacuum dried at 100 ° C. for 12 hours to obtain a polyimide powder. The intrinsic viscosity of the obtained polyimide was 0.79 dL / g. Completion of imidization was confirmed by FT-IR (FIG. 8). Table 3 shows the evaluation of the solubility of the obtained polyimide powder in each solvent.
<実施例13>
実施例12で得られたポリイミド粉末を室温でDMAcに再溶解し、12重量%の溶液を調製した。このポリイミド溶液をガラス基板上に流延し、60℃で2時間熱風乾燥器によって乾燥した。その後、ガラス基板ごと減圧下200℃で1時間乾燥した後、室温まで放冷後、ガラス基板からポリイミドフィルムを剥した。このポリイミドフィルムをもう一度減圧下で250℃1時間乾燥した。得られたフィルムの膜物性を表4に示す。
<Example 13>
The polyimide powder obtained in Example 12 was redissolved in DMAc at room temperature to prepare a 12% by weight solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was again dried under reduced pressure at 250 ° C. for 1 hour. Table 4 shows the film physical properties of the obtained film.
<実施例14>
(ポリアミド酸の重合)
式(20)で表されるジアミン0.9607g(3mmol)を脱水DMAc6.6gに溶解した。ここに式(1)で表されるテトラカルボン酸二無水物粉末1.2827g(1.8mmol)と式(19)で表されるテトラカルボン酸二無水物粉末0.6101g(1.2mmol)とをゆっくり加えて固形分濃度30重量%で撹拌した。室温で72時間撹拌しポリイミド前駆体であるポリアミド酸を得た。得られたポリアミド酸の固有粘度は、0.78dL/gであった。
<Example 14>
(Polyamide acid polymerization)
0.9607 g (3 mmol) of the diamine represented by the formula (20) was dissolved in 6.6 g of dehydrated DMAc. Here, 1.2827 g (1.8 mmol) of tetracarboxylic dianhydride powder represented by formula (1) and 0.6101 g (1.2 mmol) of tetracarboxylic dianhydride powder represented by formula (19) Was slowly added and stirred at a solid concentration of 30% by weight. The mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor. The intrinsic viscosity of the obtained polyamic acid was 0.78 dL / g.
(化学イミド化によるポリイミドの合成)
得られたポリアミド酸溶液を脱水DMAcで固形分濃度8重量%に希釈後、3.0627g(30mmmol)の無水酢酸と1.1865g(15mmol)のピリジンの混合溶液を室温でゆっくり滴下し、その後24時間撹拌した。得られたポリイミド溶液を大量の脱イオン水に加え、目的生成物を沈澱させた。得られた析出物をメタノールで十分洗浄し、100℃で12時間真空乾燥しポリイミド粉末を得た。得られたポリイミドの固有粘度は、0.84dL/gであった。イミド化の完結は、FT-IRによって確認した(図9)。得られたポリイミド粉末の各溶媒に対する溶解性評価を表3に示す。
(Polyimide synthesis by chemical imidization)
The obtained polyamic acid solution was diluted with dehydrated DMAc to a solid concentration of 8% by weight, and then a mixed solution of 3.0627 g (30 mmol) of acetic anhydride and 1.1865 g (15 mmol) of pyridine was slowly added dropwise at room temperature. Stir for hours. The resulting polyimide solution was added to a large amount of deionized water to precipitate the desired product. The obtained precipitate was sufficiently washed with methanol and vacuum dried at 100 ° C. for 12 hours to obtain a polyimide powder. The intrinsic viscosity of the obtained polyimide was 0.84 dL / g. Completion of imidization was confirmed by FT-IR (FIG. 9). Table 3 shows the evaluation of the solubility of the obtained polyimide powder in each solvent.
(ポリイミド溶液の調製およびポリイミドフィルムの作製)
得られたポリイミド粉末を室温でCPNに再溶解し、20重量%の溶液を調製した。このポリイミド溶液をガラス基板上に流延し、60℃で2時間熱風乾燥器によって乾燥した。その後、ガラス基板ごと減圧下200℃で1時間乾燥した後、室温まで放冷後、ガラス基板からポリイミドフィルムを剥した。このポリイミドフィルムをもう一度減圧下で250℃1時間乾燥した。得られたフィルムの膜物性を表4に示す。
(Preparation of polyimide solution and preparation of polyimide film)
The obtained polyimide powder was redissolved in CPN at room temperature to prepare a 20 wt% solution. This polyimide solution was cast on a glass substrate and dried by a hot air dryer at 60 ° C. for 2 hours. Then, after drying at 200 degreeC under pressure reduction for 1 hour with the glass substrate, the polyimide film was peeled from the glass substrate after standing to cool to room temperature. This polyimide film was again dried under reduced pressure at 250 ° C. for 1 hour. Table 4 shows the film physical properties of the obtained film.
<実施例15>
(ポリアミド酸の重合)
式(20)で表されるジアミン0.9607g(3mmol)を脱水DMAc6.5gに溶解した。ここに式(1)で表されるテトラカルボン酸二無水物粉末1.0689g(1.5mmol)と式(19)で表されるテトラカルボン酸二無水物粉末0.7626g(1.5mmol)とをゆっくり加えて固形分濃度30重量%で撹拌した。適宜DMAcで希釈しながら室温で72時間撹拌しポリイミド前駆体であるポリアミド酸を得た(固形分濃度28.5重量%)。得られたポリアミド酸の固有粘度は、0.83dL/gであった。
<Example 15>
(Polyamide acid polymerization)
0.9607 g (3 mmol) of the diamine represented by the formula (20) was dissolved in 6.5 g of dehydrated DMAc. Here, 1.0689 g (1.5 mmol) of tetracarboxylic dianhydride powder represented by formula (1), 0.7626 g (1.5 mmol) of tetracarboxylic dianhydride powder represented by formula (19), and Was slowly added and stirred at a solid concentration of 30% by weight. While appropriately diluted with DMAc, the mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor (solid content concentration 28.5% by weight). The resulting polyamic acid had an intrinsic viscosity of 0.83 dL / g.
(化学イミド化によるポリイミドの合成)
得られたポリアミド酸溶液を脱水DMAcで固形分濃度8重量%に希釈後、3.0627g(30mmmol)の無水酢酸と1.1865g(15mmol)のピリジンの混合溶液を室温でゆっくり滴下し、その後24時間撹拌した。得られたポリイミド溶液を大量の脱イオン水に加え、目的生成物を沈澱させた。得られた析出物をメタノールで十分洗浄し、100℃で12時間真空乾燥しポリイミド粉末を得た。得られたポリイミドの固有粘度は、0.74dL/gであった。イミド化の完結は、FT-IRによって確認した(図10)。得られたポリイミド粉末の各溶媒に対する溶解性評価を表3に示す。
(Polyimide synthesis by chemical imidization)
The obtained polyamic acid solution was diluted with dehydrated DMAc to a solid concentration of 8% by weight, and then a mixed solution of 3.0627 g (30 mmol) of acetic anhydride and 1.1865 g (15 mmol) of pyridine was slowly added dropwise at room temperature. Stir for hours. The resulting polyimide solution was added to a large amount of deionized water to precipitate the desired product. The obtained precipitate was sufficiently washed with methanol and vacuum dried at 100 ° C. for 12 hours to obtain a polyimide powder. The intrinsic viscosity of the obtained polyimide was 0.74 dL / g. Completion of imidization was confirmed by FT-IR (FIG. 10). Table 3 shows the evaluation of the solubility of the obtained polyimide powder in each solvent.
<比較例1>(ポリアミド酸の重合;DABA系)
4,4’-ジアミノベンズアニリド(DABA)0.6818g(3mmol)を脱水NMP20.6gに溶解した。ここに合成例1で合成したスピロ構造を含まないテトラカルボン酸二無水物粉末1.6033g(3mmol)をゆっくり加えて固形分濃度10.0重量%で撹拌した。室温で72時間撹拌し粘稠なポリアミド酸を得た。
<Comparative Example 1> (Polyamide acid polymerization; DABA system)
0.6818 g (3 mmol) of 4,4′-diaminobenzanilide (DABA) was dissolved in 20.6 g of dehydrated NMP. To this, 1.6033 g (3 mmol) of tetracarboxylic dianhydride powder containing no spiro structure synthesized in Synthesis Example 1 was slowly added and stirred at a solid content concentration of 10.0% by weight. The mixture was stirred at room temperature for 72 hours to obtain a viscous polyamic acid.
(化学イミド化によるポリイミドの合成)
得られたポリアミド酸溶液を脱水NMPで固形分濃度8重量%に希釈後、3.0627g(30mmmol)の無水酢酸と1.1865g(15mmol)のピリジンの混合溶液を室温でゆっくり滴下したところ、ゲル化が生じ反応を中断した。これは、高分子中にスピロ構造を含まないために、溶媒に対する溶解性が不十分となりゲル化したと考えられる。
(Polyimide synthesis by chemical imidization)
After the obtained polyamic acid solution was diluted with dehydrated NMP to a solid content concentration of 8% by weight, a mixed solution of 3.0627 g (30 mmol) of acetic anhydride and 1.1865 g (15 mmol) of pyridine was slowly added dropwise at room temperature. The reaction was interrupted. This is presumably because the polymer does not contain a spiro structure, so that its solubility in a solvent is insufficient and gelation occurs.
<比較例2>(ポリアミド酸の重合;4,4’‐ODA系)
4,4’-オキシジアニリン(4,4’-ODA)0.6007g(3mmol)を脱水NMP19.8gに溶解した。ここに合成例1で合成したスピロ構造を含まないテトラカルボン酸二無水物粉末1.6033g(3mmol)をゆっくり加えて固形分濃度10.0重量%で撹拌した。室温で72時間撹拌し粘稠なポリアミド酸を得た。
<Comparative Example 2> (Polyamide acid polymerization; 4,4′-ODA system)
0.6007 g (3 mmol) of 4,4′-oxydianiline (4,4′-ODA) was dissolved in 19.8 g of dehydrated NMP. To this, 1.6033 g (3 mmol) of tetracarboxylic dianhydride powder containing no spiro structure synthesized in Synthesis Example 1 was slowly added and stirred at a solid content concentration of 10.0% by weight. The mixture was stirred at room temperature for 72 hours to obtain a viscous polyamic acid.
(化学イミド化によるポリイミドの合成)
得られたポリアミド酸溶液を脱水NMPで固形分濃度3重量%に希釈後、3.0627g(30mmmol)の無水酢酸と1.1865g(15mmol)のピリジンの混合溶液を室温でゆっくり滴下したところ、ゲル化が生じ反応を中断した。これは、高分子中にスピロ構造を含まないために、溶媒に対する溶解性が不十分となりゲル化したと考えられる。
(Polyimide synthesis by chemical imidization)
After the obtained polyamic acid solution was diluted with dehydrated NMP to a solid content concentration of 3% by weight, a mixed solution of 3.0627 g (30 mmol) of acetic anhydride and 1.1865 g (15 mmol) of pyridine was slowly added dropwise at room temperature. The reaction was interrupted. This is presumably because the polymer does not contain a spiro structure, so that its solubility in a solvent is insufficient and gelation occurs.
<比較例3>(ポリアミド酸の重合;TFMB系)
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)0.9607g(3mmol)を脱水N,N-ジメチルアセトアミド(DMAc)6.0gに溶解した。ここに合成例1で合成したスピロ構造を含まないテトラカルボン酸二無水物粉末1.6033g(3mmol)とをゆっくり加えて固形分濃度30重量%で撹拌した。適宜DMAcで希釈しながら室温で72時間撹拌しポリイミド前駆体であるポリアミド酸を得た(固形分濃度18.1重量%)。得られたポリアミド酸の固有粘度は、2.26dL/gであった。
<Comparative Example 3> (Polyamide acid polymerization; TFMB system)
0.9607 g (3 mmol) of 4,4′-diamino-2,2′-bis (trifluoromethyl) biphenyl (TFMB) was dissolved in 6.0 g of dehydrated N, N-dimethylacetamide (DMAc). To this, 1.6033 g (3 mmol) of tetracarboxylic dianhydride powder containing no spiro structure synthesized in Synthesis Example 1 was slowly added and stirred at a solid content concentration of 30% by weight. While appropriately diluted with DMAc, the mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor (solid content concentration: 18.1% by weight). The obtained polyamic acid had an intrinsic viscosity of 2.26 dL / g.
(化学イミド化によるポリイミドの合成)
得られたポリアミド酸溶液の半分を脱水DMAcで固形分濃度8重量%に希釈後、1.5314g(15mmmol)の無水酢酸と0.5932g(7.5mmol)のピリジンの混合溶液を室温でゆっくり滴下したところ、溶液の流動性がなくなり、ゲル化したため、反応を中断した。これは、高分子中にスピロ構造を含まないために、溶媒に対する溶解性が不十分となりゲル化したと考えられる。
(Polyimide synthesis by chemical imidization)
Half of the obtained polyamic acid solution was diluted with dehydrated DMAc to a solid concentration of 8% by weight, and then a mixed solution of 1.5314 g (15 mmol) acetic anhydride and 0.5932 g (7.5 mmol) pyridine was slowly added dropwise at room temperature. As a result, the fluidity of the solution disappeared and gelation occurred, so the reaction was interrupted. This is presumably because the polymer does not contain a spiro structure, so that its solubility in a solvent is insufficient and gelation occurs.
<比較例4>
(ポリアミド酸の重合)
式(20)で表されるジアミン0.9607g(3mmol)を脱水N,N-ジメチルアセトアミド(DMAc)6.0gに溶解した。ここに式(18)で表されるテトラカルボン酸二無水物粉末1.6033g(3mmol)とをゆっくり加えて固形分濃度30重量%で撹拌した。適宜DMAcで希釈しながら室温で72時間撹拌しポリイミド前駆体であるポリアミド酸を得た(固形分濃度18.1重量%)。得られたポリアミド酸の固有粘度は、2.26dL/gであった。
<Comparative example 4>
(Polyamide acid polymerization)
0.9607 g (3 mmol) of the diamine represented by the formula (20) was dissolved in 6.0 g of dehydrated N, N-dimethylacetamide (DMAc). To this, 1.6033 g (3 mmol) of tetracarboxylic dianhydride powder represented by the formula (18) was slowly added and stirred at a solid content concentration of 30% by weight. While appropriately diluted with DMAc, the mixture was stirred at room temperature for 72 hours to obtain a polyamic acid as a polyimide precursor (solid content concentration: 18.1% by weight). The obtained polyamic acid had an intrinsic viscosity of 2.26 dL / g.
(化学イミド化によるポリイミドの合成)
得られたポリアミド酸溶液の半分を脱水DMAcで固形分濃度8重量%に希釈後、1.5314g(15mmmol)の無水酢酸と0.5932g(7.5mmol)のピリジンの混合溶液を室温でゆっくり滴下したところ、溶液の流動性がなくなり、ゲル化したため、反応を中断した。これは、高分子中にスピロ構造を含まないために、溶媒に対する溶解性が不十分となりゲル化したと考えられる。
(Polyimide synthesis by chemical imidization)
Half of the obtained polyamic acid solution was diluted with dehydrated DMAc to a solid concentration of 8% by weight, and then a mixed solution of 1.5314 g (15 mmol) acetic anhydride and 0.5932 g (7.5 mmol) pyridine was slowly added dropwise at room temperature. As a result, the fluidity of the solution disappeared and gelation occurred, so the reaction was interrupted. This is presumably because the polymer does not contain a spiro structure, so that its solubility in a solvent is insufficient and gelation occurs.
Claims (8)
で表される繰り返し単位を有するポリイミド。 The following general formula (2):
The polyimide which has a repeating unit represented by these.
(A)波長400nmにおける光透過率が30%以上;
(B)線熱膨張係数が40ppm/K以下;
(C)ガラス転移温度(Tg)が260℃以上。 The polyimide film containing the polyimide copolymer according to claim 3 or 4 having the following characteristics (A), (B) and (C):
(A) The light transmittance at a wavelength of 400 nm is 30% or more;
(B) the coefficient of linear thermal expansion is 40 ppm / K or less;
(C) Glass transition temperature (Tg) is 260 ° C. or higher.
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| JPWO2021085319A1 (en) * | 2019-10-29 | 2021-05-06 | ||
| JP2021185165A (en) * | 2017-03-31 | 2021-12-09 | 田岡化学工業株式会社 | Polyimide having fluorene skeleton |
| WO2023276888A1 (en) * | 2021-07-01 | 2023-01-05 | 株式会社カネカ | Polyamic acid, polyamic acid composition, polyimide, polyimide film, laminate, production method for laminate, and electronic device |
| WO2023074350A1 (en) * | 2021-10-25 | 2023-05-04 | 株式会社カネカ | Polyamide acid, polyamide acid composition, polyimide, polyimide film, multilayer body, method for producing multilayer body, and electronic device |
| JP2024536174A (en) * | 2021-09-30 | 2024-10-04 | ピーアイ・アドバンスド・マテリアルズ・カンパニー・リミテッド | Polyimide powder and its manufacturing method |
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| KR102347634B1 (en) * | 2019-11-13 | 2022-01-10 | 피아이첨단소재 주식회사 | High Adhesion and Low Dielectric Polyimide Film and Manufactufing Mehtod Thereof |
| KR102347632B1 (en) * | 2019-11-13 | 2022-01-10 | 피아이첨단소재 주식회사 | Low Dielectric Polyimide Film and Manufacutring Method Thereof |
| KR102788044B1 (en) * | 2020-07-13 | 2025-03-31 | 에스케이이노베이션 주식회사 | Polyimide precursor, its solution, polyimide film, manufacturing method thereof, and use thereof |
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| JP2021185165A (en) * | 2017-03-31 | 2021-12-09 | 田岡化学工業株式会社 | Polyimide having fluorene skeleton |
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| WO2023276888A1 (en) * | 2021-07-01 | 2023-01-05 | 株式会社カネカ | Polyamic acid, polyamic acid composition, polyimide, polyimide film, laminate, production method for laminate, and electronic device |
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