CN108117655A - Method for producing polyimide film, and polyimide film - Google Patents

Method for producing polyimide film, and polyimide film Download PDF

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Publication number
CN108117655A
CN108117655A CN201710535303.7A CN201710535303A CN108117655A CN 108117655 A CN108117655 A CN 108117655A CN 201710535303 A CN201710535303 A CN 201710535303A CN 108117655 A CN108117655 A CN 108117655A
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polyimide film
manufacturing
film according
monomer
inorganic particle
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孙德峥
许艳惠
陈启盛
李国维
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Mortech Corp
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Mortech Corp
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G73/00Macromolecular 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
    • C08G73/06Polycondensates having nitrogen-containing heterocyclic rings in the main chain of the macromolecule
    • C08G73/10Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
    • C08G73/1067Wholly aromatic polyimides, i.e. having both tetracarboxylic and diamino moieties aromatically bound
    • C08G73/1071Wholly aromatic polyimides containing oxygen in the form of ether bonds in the main chain
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/28Nitrogen-containing compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/38Boron-containing compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2379/00Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen, or carbon only, not provided for in groups C08J2361/00 - C08J2377/00
    • C08J2379/04Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
    • C08J2379/08Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • C08K2003/2227Oxides; Hydroxides of metals of aluminium
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/28Nitrogen-containing compounds
    • C08K2003/282Binary compounds of nitrogen with aluminium
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/38Boron-containing compounds
    • C08K2003/382Boron-containing compounds and nitrogen
    • C08K2003/385Binary compounds of nitrogen with boron

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  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
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Abstract

The invention discloses a method for manufacturing a polyimide film and the polyimide film. Then, the polyamic acid mixture is heated at a drying temperature to form a polyamic acid film. Subsequently, the polyamic acid film is imidized to form a polyimide film. The weight percentage of the inorganic particles is 10 wt% to 50 wt% relative to the total weight of the inorganic particles, the diamine monomer and the tetracarboxylic dianhydride monomer, and the thermal conductivity of the polyimide film is greater than or equal to 0.4W/mK.

Description

The manufacturing method and polyimide film of polyimide film
Technical field
Manufacturing method and polyimide film of the present invention on a kind of polyimide film have good especially with regard to one kind The manufacturing method and polyimide film of the polyimide film of thermal conductivity.
Background technology
Polyimides has the high molecular material of excellent mechanical performance, heat resistance and chemical resistance.Therefore, Polyimides is widely used in flexible printed wiring board, such as mobile phone, camera model, touch panel module, liquid crystal display All there is use in panel and tablet computer.However, electronic component can generate heat at work, excessive accumulation of heat can be led It is excessively high to send a telegraph sub- product internal temperature, causes component wear, therefore the technology for improving electronic element radiating characteristic is taken seriously.
Due to polyimide film in itself have good heat resistance but thermal conductivity it is more bad, how to promote polyimides The problem of thermal conductivity of film is to improve the accumulation of heat of flexible printed wiring board will be the current industry problem to be overcome.
The content of the invention
In view of the above problems, the present invention provides a kind of manufacturing method and polyimide film of polyimide film, so as to carrying The thermal conductivity of polyimide film is risen, to solve the problems, such as to accumulate heat on flexible printed wiring board.
The present invention discloses a kind of manufacturing method of polyimide film, and it includes formation to include an inorganic particle, a diamines One polyamic acid mixture of monomer and tetracarboxylic dianhydride's monomer.Then, polyamic acid mixture is heated with a drying temperature Form a polyamide acid film.Then, polyamide acid film is subjected to a sub- amidation process and forms a polyimide film.Wherein, phase For the total weight of inorganic particle, diamine monomer and tetracarboxylic dianhydride's monomer, the weight percent of inorganic particle for 10wt% extremely 50wt%, the thermal conductivity coefficient of polyimide film are more than or equal to 0.4W/mK.
The present invention also discloses a kind of PA membrane as obtained by the above method.
The manufacturing method and PA membrane of polyimide film according to the invention described above, due to compared with inorganic particulate The total weight of grain, diamine monomer and tetracarboxylic dianhydride's monomer, the weight percent of inorganic particle is 10wt% to 50wt%, thus The problem of heat is accumulated on flexible printed wiring board can be improved.Thus, as poly- obtained by sub- amidation polyamide acid film Acid imide film can have high-termal conductivity, the problem that solving in the prior art.
The explanation of explanation and implementation below above with respect to present invention to demonstrate and explain the present invention original Reason, and the claims for providing the present invention are further explained.
Description of the drawings
Fig. 1 is the flow chart of the polyimides film manufacturing method of one embodiment of the invention.
Specific embodiment
The detailed features and advantage of the narration present invention, content are enough to make any ability in detail in embodiments below The technical staff in domain understands the technology contents of the present invention and implements according to this, and is wanted according to content disclosed in this specification, right Protection domain and attached drawing are asked, any those skilled in the art can be readily understood upon the relevant purpose of the present invention and advantage.Below Embodiment the viewpoint of the present invention is further described, it is but non-anyways to limit scope of the invention.
The production method for first introducing the polyimide film of the present invention below, refer to Fig. 1.Fig. 1 is one embodiment of the invention Polyimide film production method flow chart.
One inorganic particle is added in a solvent and is uniformly mixed and forms a suspension (S101).
Specifically, solvent may be selected from dimethylformamide (N, N-Dimethyl formamide;DMF), dimethyl second Amide (Dimethylacetamide;DMAc), dimethyl sulfoxide (DMSO) (Dimethyl sulfoxide;DMSO), N- methyl -2- pyrroles Pyrrolidone (N-methyl-2-pyrrolidone;) and its group that is formed NMP.The grain size of inorganic particle can be 0.1 micro- Rice is to 5 microns.Inorganic particle is selected from aluminium oxide, boron nitride, zinc oxide, aluminium nitride, barium titanate and its group formed.It can borrow By stirring inorganic particle is made to uniformly disperse in a solvent, to form suspension.Any mode or means that can reach stirring Applied in the present invention.
Then, a diamine monomer and tetracarboxylic dianhydride's monomer are added in suspension and be uniformly mixed and form a polyamic acid Mixture.
Specifically, diamine monomer is selected from p-phenylenediamine (Isosorbide-5-Nitrae-diamino benzene), m-phenylene diamine (MPD) (1,3- Diamino benzene), 4,4'- diaminodiphenyl ethers (4,4'-oxydianiline), 3,4'- diaminodiphenyl ethers (3,4'- Oxydianiline), 4,4'- diamino hexichol alkane (4,4'-methylene dianiline), DPD di p phenylenediamine (N, N- Diphenylethylenediamine), diamino benzophenone (diaminobenzophenone), diamines diphenyl sulfone (diamino diphenyl sulfone), two naphthylenediamines (1,5-naphthalene diamine), diaminodiphenyl sulfide Double (the 3- amino phenols oxygroup) benzene (1,3-Bis (3- of (4,4'-diamino diphenyl sulfide), 1,3- Aminophenoxy) benzene), double (the 4- amino phenols oxygroup) benzene (1,4-Bis (4-aminophenoxy) benzene) of 1,4-, Double (the 4- amino phenols oxygroup) benzene (1,3-Bis (4-aminophenoxy) benzene) of 1,3-, double [4- (the 4- amino phenols oxygen of 2,2- Base) phenyl] propane (2,2-Bis [4- (4-amino phenoxy) phenyl] propane), 4,4'- double (4- amino phenols oxygroup) Double (the 3- amino phenols oxygroup) biphenyl (4,4'-bis- of biphenyl (4,4'-bis- (4-aminophenoxy) biphenyl), 4,4'- (3-aminophenoxy) biphenyl), 1,3- dipropyl amido -1,1', 3,3'- tetramethyl disiloxanes (1,3-Bis (3- Aminopropyl) -1,1', 3,3'-tetramethyldisiloxane), 1,3- dipropyl amido -1,1', 3,3'- tetraphenyl two Siloxanes (1,3-Bis (3-aminopropyl) -1,1', 3,3'-tetraphenyldisiloxane), 1,3- dipropyls amido - 1,1- dimethyl -3,3- diphenyl disiloxane (1,3-Bis (aminopropyl) - ) and its group that is formed dimethyldiphenyldisiloxane.
Tetracarboxylic dianhydride's monomer is selected from pyromellitic acid anhydride (1,2,4,5Benzene tetracarboxylic Dianhydride), biphenyl tetracarboxylic dianhydride (3,3', 4,4'-Biphenyl tetracarboxylic dianhydride), Oxydiphthalic (4,4'-Oxydiphthalic anhydride), benzophenone tetracarboxylic dianhydride (Benzophenonetetracarboxylic dianhydride), diphenyl sulfone tetracarboxylic dianhydride (3,3', 4,4'- Diphenyl sulfonetetracarboxylic dianhydride), naphthalene tetracarboxylic dianhydride (1,2,5,6-naphthalene Tetracarboxylic dianhydride), naphthalene dicarboxylic anhydride (Naphthalenetetracaboxylic Dianhydride), Double-(3,4- phthalate anhydrides) dimethylsilane (bis (3,4-dicarboxyphenyl) dimethylsilane Dianhydride), 1,3- double (3,4- dicarboxyphenyis) -1,1', 3,3'- tetramethyl disiloxanes dianhydride (1,3-bis (3,4- Phthalic anhydride)-tetramethyldisiloxane) and its group that is formed.Wherein, diamine monomer and four The molar ratio of carboxylic acid dianhydride monomer can be 0.98:1 to 1.05:1.
Specifically, the step of forming polyamic acid mixture further includes the following steps.
Diamine monomer is added in, a mixture (S102) containing diamine monomer is formed in suspension.
Then, tetracarboxylic dianhydride's monomer is incorporated in formation polyamic acid mixture in the mixture containing diamine monomer (S103)。
But the order of present invention addition diamine monomer and tetracarboxylic dianhydride's monomer can also be such as following step.
Tetracarboxylic dianhydride's monomer is added in, a mixture containing tetracarboxylic dianhydride's monomer is formed in suspension.
Then, diamine monomer is added in and polyamic acid mixture is formed in the mixture containing tetracarboxylic dianhydride's monomer.
Furthermore polyamic acid mixture is coated on a base material (S104).
Specifically, base material can be a supporting steel band or roller etc., but be not limited thereto.As for used coating side Method, any existing coating technique is applied both to the present invention, such as slot coated method (slit coating) or mould can be used Has rubbing method (die coating).
Then, heat drying polyamic acid mixture forms a polyamide acid film (S105).
Specifically, be coated with polyamic acid mixture base material be positioned in 120 DEG C to 200 DEG C of hot environment into Row heat drying.Thus, which the solvent in polyamic acid mixture is left polyamic acid mixture by thermal evaporation, and make Not vaporized polyamic acid mixture forms polyamide acid film.After the solvent in polyamic acid mixture by after thermal evaporation, By polyamide acid film peeling base, polyamide acid film is obtained.One drying temperature of heat drying can be matched with the boiling point of solvent. In section Example of the present invention, drying temperature is 120 DEG C to 200 DEG C, but is not limited thereto.
Uniaxial extension polyamide acid film is carried out at the same time sub- amidation process and forms polyimide film (S106).
Specifically, 0.05MPa (N/mm are applied to polyamide acid film2) to 0.5MPa (N/mm2) a uniaxial tension Power makes polyamide acid film uniaxially carrying out sub- amidation process along in the state of stretching to form polyimide film.Sub- amidation (imidization) reaction can be higher than the temperature of heat drying polyamide acid film is heated, and make polyamide garden sorrel In polyamic acid dehydration and endless loop and form polyimide film.Sub- amidation process can also be added in polyamic acid Dehydrating agent (such as:Acid anhydrides) or catalyst (polymer icarceration type catalyst) polyamic acid in polyamide garden sorrel is made to be dehydrated and dead It cycles (chemical imidization method) and forms polyimide film.Wherein, heating temperature is higher, and polyamide acid film carries out sub- amidation (imidization) time needed for reaction generation polyimide film is shorter.However, if the temperature of reaction is excessively high, then may The bond between the atom in polyimide molecule can be destroyed so that polyimides is degraded (degradation) because of high temperature. In section Example of the present invention, heating makes the temperature of the sub- amidation process of polyamide acid film progress be 250 DEG C to 450 DEG C, but It is not limited thereto.
Uniaxial extension refers to the tensile stress that a direction is substantially only bestowed to polyamide acid film, and in tensile stress side To vertical direction on, tension substantially is not bestowed to polyamide acid film.In an embodiment of the present invention, the polyamides formed Amino acid film is a strip winding shape, and heating stepses are that polyamide acid film is allowed slowly to pass through high temperature furnace.Therefore, implementation of the invention In example, the direction of uniaxial extension is parallel to the moving direction of polyamide acid film, that is, uniaxial extension is oriented parallel to polyamides The long side direction of amino acid film, but not limited to this.In the other embodiment of the present invention, the direction of uniaxial extension is selected from polyamide The either side of sorrel to.
It is inorganic compared with the total weight of the inorganic particle, the diamine monomer and tetracarboxylic dianhydride's monomer in the present embodiment The weight percent of particle is 10wt% to 50wt%, preferably 20wt% to 35wt%, is more preferably 23wt% to 31.5wt%. If inorganic particle is more than in the total weight content compared with the inorganic particle, the diamine monomer and tetracarboxylic dianhydride's monomer 50wt%, the then easy embrittlement of polyimide film increase cut-off knife consume without easily molded or polyimide film bad cut really up to the mark. If inorganic particle content in compared with the total weight of the inorganic particle, the diamine monomer with tetracarboxylic dianhydride's monomer is less than 10wt%, then the heat dissipation effect of polyimide film is not notable.Furthermore the thermal conductivity coefficient of polyimide film is more than or equal to 0.4W/mK, Preferably 0.45W/mK to 0.75W/mK.
Illustrate the manufacturing method of PA membrane disclosed in the present application below by way of several embodiments and comparative example, and into Row experiment test is to compare its nature difference.
Comparative example 1
The 4,4'- diamino two of 96.23g is added in the dimethyl acetamide (DMAc) (purity 99.95wt%) of 800g Phenylate (ODA), and stirred to dissolve.
Secondly, add in the pyromellitic acid anhydride (PDMA) of 103.77g, and stir 6 it is small when to carry out polymerisation, and obtain To polyamic acid mixture.The temperature of polymerisation is controlled at 20 DEG C to 30 DEG C.
Then, polyamic acid mixture is coated on base material.Then, it is dried 10 minutes at 150 DEG C of temperature, it will Polyamic acid mixture obtains the polyamide acid film that thickness is 12.5 microns to 75 microns by being removed on base material.
Furthermore in the state of uniaxial extension polyamide acid film, heat polyamide acid film 10 minutes with 300 DEG C, carry out sub- Amidation process, and obtain polyimide film.The long side direction for being oriented parallel to polyamide acid film of uniaxial extension, is applied to poly- The uniaxially pulling force of amide sorrel is 0.1MPa (0.1N/mm2)。
Embodiment 1-1
The aluminium oxide of 49.63g is added in the dimethyl acetamide (DMAc) (purity 99.95wt%) of 800g, it then, will Dimethylacetamide solution is uniformly mixed to form suspension.
Secondly, in suspension add in 72.35g 4,4'- diaminodiphenyl ethers (ODA), and be uniformly mixed make its dissolving.
Then, add in the pyromellitic acid anhydride (PDMA) of 78.02g, and stir 6 it is small when to carry out polymerisation, and obtain To polyamic acid mixture.The temperature of polymerisation is controlled at 20 DEG C to 30 DEG C.Next drying and forming-film, sub- amidation, list Axis extension is identical with comparative example one, just repeats no more herein.
Embodiment 1-2
The step of embodiment 1-2, is similar to embodiment 1-1, and embodiment 1-2 is in embodiment 1-1 differences in poly- sub- acyl Aminating process fixed form is different, and the corner of polyimide film in the stationary state, polyamides is heated with 300 DEG C by embodiment 1-2 Amino acid film 10 minutes carries out sub- amidation process, and obtains polyimide film.
Embodiment 2-1
The aluminium oxide and 4.41g of 48.53g is added in the dimethyl acetamide (DMAc) (purity 99.95wt%) of 800g Boron nitride, then, dimethylacetamide solution is uniformly mixed to form suspension.
Secondly, in suspension add in 70.76g 4,4'- diaminodiphenyl ethers (ODA), and be uniformly mixed make its dissolving.
Then, add in the pyromellitic acid anhydride (PDMA) of 76.3g, and stir 6 it is small when to carry out polymerisation, and obtain Polyamic acid mixture.The temperature of polymerisation is controlled at 20 DEG C to 30 DEG C.Next drying and forming-film, sub- amidation, single shaft Extension is identical with comparative example one, just repeats no more herein.
Embodiment 2-2
The step of embodiment 2-2, is similar to embodiment 2-1, and embodiment 2-2 is in embodiment 2-1 differences in poly- sub- acyl Aminating process fixed form is different, and the corner of polyimide film in the stationary state, polyamides is heated with 300 DEG C by embodiment 2-2 Amino acid film 10 minutes carries out sub- amidation process, and obtains polyimide film.
Embodiment 3-1
The aluminium oxide and 8.63g of 47.48g is added in the dimethyl acetamide (DMAc) (purity 99.95wt%) of 800g Boron nitride, then, dimethylacetamide solution is uniformly mixed to form suspension.
Secondly, in suspension add in 69.23g 4,4'- diaminodiphenyl ethers (ODA), and be uniformly mixed make its dissolving.
Then, add in the pyromellitic acid anhydride (PDMA) of 74.66g, and stir 6 it is small when to carry out polymerisation, and obtain To polyamic acid mixture.The temperature of polymerisation is controlled at 20 DEG C to 30 DEG C.Next drying and forming-film, sub- amidation, list Axis extension is identical with comparative example one, just repeats no more herein.
Embodiment 3-2
The step of embodiment 3-2, is similar to embodiment 3-1, and embodiment 3-2 is in embodiment 3-1 differences in poly- sub- acyl Aminating process fixed form is different, and the corner of polyimide film in the stationary state, polyamides is heated with 300 DEG C by embodiment 3-2 Amino acid film 10 minutes carries out sub- amidation process, and obtains polyimide film.
Embodiment 4-1
The aluminium oxide and 12.68g of 46.47g is added in the dimethyl acetamide (DMAc) (purity 99.95wt%) of 800g Boron nitride, then, dimethylacetamide solution is uniformly mixed to form suspension.
Secondly, in suspension add in 67.77g 4,4'- diaminodiphenyl ethers (ODA), and be uniformly mixed make its dissolving.
Then, add in the pyromellitic acid anhydride (PDMA) of 73.08g, and stir 6 it is small when to carry out polymerisation, and obtain To polyamic acid mixture.The temperature of polymerisation is controlled at 20 DEG C to 30 DEG C.Next drying and forming-film, sub- amidation, list Axis extension is identical with comparative example one, just repeats no more herein.
Embodiment 4-2
The step of embodiment 4-2, is similar to embodiment 4-1, and embodiment 4-2 is in embodiment 4-1 differences in poly- sub- acyl Aminating process fixed form is different, and the corner of polyimide film in the stationary state, polyamides is heated with 300 DEG C by embodiment 4-2 Amino acid film 10 minutes carries out sub- amidation process, and obtains polyimide film.
Embodiment 5-1
The aluminium oxide and 16.55g of 45.52g is added in the dimethyl acetamide (DMAc) (purity 99.95wt%) of 800g Boron nitride, then, dimethylacetamide solution is uniformly mixed to form suspension.
Secondly, in suspension add in 66.36g 4,4'- diaminodiphenyl ethers (ODA), and be uniformly mixed make its dissolving.
Then, add in the pyromellitic acid anhydride (PDMA) of 71.57g, and stir 6 it is small when to carry out polymerisation, and obtain To polyamic acid mixture.The temperature of polymerisation is controlled at 20 DEG C to 30 DEG C.Next drying and forming-film, sub- amidation, list Axis extension is identical with comparative example one, just repeats no more herein.
Embodiment 5-2
The step of embodiment 5-2, is similar to embodiment 5-1, and embodiment 5-2 is in embodiment 5-1 differences in poly- sub- acyl Aminating process fixed form is different, and the corner of polyimide film in the stationary state, polyamides is heated with 300 DEG C by embodiment 5-2 Amino acid film 10 minutes carries out sub- amidation process, and obtains polyimide film.
Embodiment 6
The boron nitride of 49.63g is added in the dimethyl acetamide (DMAc) (purity 99.95wt%) of 800g, it then, will Dimethylacetamide solution is uniformly mixed to form suspension.
Secondly, 4, the 4'- diaminodiphenyl ethers (ODA) of 47.62g and the p-phenylenediamine of 17.14g are added in suspension (PPDA), and be uniformly mixed make its dissolving.
Then, add in the pyromellitic acid anhydride (PDMA) of 85.61g, and stir 6 it is small when to carry out polymerisation, and obtain To polyamic acid mixture.The temperature of polymerisation is controlled at 20 DEG C to 30 DEG C.Next drying and forming-film, sub- amidation, list Axis extension is identical with comparative example one, just repeats no more herein.
Embodiment 7
The boron nitride of 57.14g is added in the dimethyl acetamide (DMAc) (purity 99.95wt%) of 800g, the person of connecing will Dimethylacetamide solution is uniformly mixed to form suspension.
Secondly, in suspension add in 67.73g 4,4'- diaminodiphenyl ethers (ODA), and be uniformly mixed make its dissolving.
Then, add in the pyromellitic acid anhydride (PDMA) of 74.12g, and stir 6 it is small when to carry out polymerisation, and obtain To polyamic acid mixture.The temperature of polymerisation is controlled at 20 DEG C to 30 DEG C.Next drying and forming-film, sub- amidation, list Axis extension is identical with comparative example one, just repeats no more herein.
Embodiment 8
The aluminium oxide and 16.55g of 45.52g is added in the dimethyl acetamide (DMAc) (purity 99.95wt%) of 800g Zinc oxide, dimethylacetamide solution is uniformly mixed to form suspension by the person of connecing.
Secondly, in suspension add in 66.36g 4,4'- diaminodiphenyl ethers (ODA), and be uniformly mixed make its dissolving.
Then, add in the pyromellitic acid anhydride (PDMA) of 71.57g, and stir 6 it is small when to carry out polymerisation, and obtain To polyamic acid mixture.The temperature of polymerisation is controlled at 20 DEG C to 30 DEG C.Next drying and forming-film, sub- amidation, list Axis extension is identical with comparative example one, just repeats no more herein.
Embodiment 9
The aluminium nitride of 49.63g is added in the dimethyl acetamide (DMAc) (purity 99.95wt%) of 800g, it then, will Dimethylacetamide solution is uniformly mixed to form suspension.
Secondly, in suspension add in 72.35g 4,4'- diaminodiphenyl ethers (ODA), and be uniformly mixed make its dissolving.
Then, add in the pyromellitic acid anhydride (PDMA) of 78.02g, and stir 6 it is small when to carry out polymerisation, and obtain To polyamic acid mixture.The temperature of polymerisation is controlled at 20 DEG C to 30 DEG C.Next drying and forming-film, sub- amidation, list Axis extension is identical with comparative example one, just repeats no more herein.
Embodiment 10
The barium titanate of 49.63g is added in the dimethyl acetamide (DMAc) (purity 99.95wt%) of 800g, then, is mixed Conjunction is formed uniformly suspension.
Secondly, in suspension add in 72.35g 4,4'- diaminodiphenyl ethers (ODA), and be uniformly mixed make its dissolving.
Then, add in the pyromellitic acid anhydride (PDMA) of 78.02g, and stir 6 it is small when to carry out polymerisation, and obtain To polyamic acid mixture.The temperature of polymerisation is controlled at 20 DEG C to 30 DEG C.Next drying and forming-film, sub- amidation, list Axis extension is identical with comparative example one, just repeats no more herein.
Table one is referred to, table one forms for the polyimide component of 15 embodiments of the invention and a comparative example, is solid Determine mode and its Correlated Case with ARMA Measurement result.
Table one
Comparative example 1 measures the thermal conductivity coefficient of the polyimide film come under conditions of no added any inorganic particle Less than 0.4W/mK, the problem of by causing heat dissipation effect bad.Embodiment 1-1 to embodiment 10 addition inorganic particle polyamides In imines film, the thermal conductivity coefficient measured is all more than 0.4W/mK, there is preferable heat dissipation effect.
Embodiment 1-1, embodiment 2-1, embodiment 3-1, the inorganic matter adding proportion point of embodiment 4-1 and embodiment 5-1 It is not identical with embodiment 1-2, embodiment 2-2, embodiment 3-2, embodiment 4-2 and embodiment 5-2, poly- sub- acyl is only that at difference Aminating process fixed form.Embodiment 1-1, embodiment 2-1, embodiment 3-1, the polyimide of embodiment 4-1 and embodiment 5-1 Change process fixed form is uniaxial extension, embodiment 1-2, embodiment 2-2, embodiment 3-2, embodiment 4-2 and embodiment 5-2 Polyimide process fixed form is by the Corner Strapped of polyimide film.Polyimide is understood by the measurement of table one When process fixed form is uniaxial extension, polyimide film can obtain higher thermal conductivity coefficient, it is possible to provide preferable heat dissipation effect.
Embodiment 1-1 to the 4,4'- diaminodiphenyl ethers of embodiment 10, pyromellitic acid anhydride and inorganic particle gross weight Measure as 200 g, the computational methods of adding proportion (wt%) for inorganic particle weight (g) divided by 200 g multiplied by with 100% and obtain.
The inorganic particle added in embodiment 1-1 be aluminium oxide, embodiment 2-1, embodiment 3-1, embodiment 4-1 and reality It is respectively aluminium oxide and boron nitride to apply the inorganic particle added in a 5-1, wherein, embodiment 1-1, embodiment 2-1, embodiment The aluminium oxide additive amount of 3-1, embodiment 4-1 and embodiment 5-1 be respectively 49.63g, 48.53g, 47.48g, 46.47g and 45.52g, embodiment 2-1, embodiment 3-1, embodiment 4-1, the nitridation Boron addition of embodiment 5-1 be respectively 4.41g, 8.63g, 12.68g and 16.55g.Understand that boron nitride adding proportion gets over high available in polyimide film by the measurement of table one Higher thermal conductivity coefficient provides preferable heat dissipation effect.
In embodiment 1-1, embodiment 6, embodiment 9 and embodiment 10, the adding proportion of inorganic particle is all 24.81wt% And the inorganic particle of single kind is only added, the thermal conductivity system of the polyimide film of addition boron nitride is understood by the measurement of table one Number highest.The inorganic particle adding proportion of embodiment 5-1 and embodiment 8 is 31.03wt%, and embodiment 5-1 is added inorganic Particle is aluminium oxide and boron nitride, and the inorganic particle that embodiment 8 is added is aluminium oxide, understands to implement by the measurement of table one The thermal conductivity coefficient of example 5-1 compares 8 higher of embodiment.Therefore, the content for understanding inorganic particle by upper result can all be influenced with species The thermal conductivity coefficient of polyimide film.
The manufacturing method and polyimide film of polyimide film according to the invention described above, add inorganic particle Polyimide film can obtain some higher thermal conductivity coefficient, provide preferable heat dissipation effect.Thus, soft printing in the prior art The problem of heat is accumulated on circuit board, causes electronic circuit component the problem of heat dissipation effect is bad occur and is just resolved.
Furthermore when the fixed form during polyamide acid film progress polyimide is uniaxial extension, polyimide film Higher thermal conductivity coefficient can be obtained, it is possible to provide preferable heat dissipation effect.Thus, it is only necessary to which relatively low inorganic particle additive amount is taken Polyimide processing procedure with uniaxial extension is that can obtain being equivalent to the poly- of higher inorganic particle additive amount collocation Corner Strapped The high thermal conductivity coefficient that sub- amidation processing procedure is reached.Thereby, the additive amount of inorganic particle can be reduced, is obtained in making with high fever While leading the polyimide film of coefficient, retain the machines such as high ductibility, high-tensile and the pliability of script polyimide film Tool property.
Certainly, the present invention can also have other various embodiments, without deviating from the spirit and substance of the present invention, ripe It knows those skilled in the art and makes various corresponding changes and deformation, but these corresponding changes and change in accordance with the present invention Shape should all belong to the protection domain of appended claims of the invention.

Claims (16)

1. a kind of manufacturing method of polyimide film, which is characterized in that including:
Form the polyamic acid mixture for including an inorganic particle, a diamine monomer and tetracarboxylic dianhydride's monomer;
The polyamic acid mixture is heated with a drying temperature and forms a polyamide acid film;And
The polyamide acid film is subjected to a sub- amidation process and forms a polyimide film;
Wherein compared with the total weight of the inorganic particle, the diamine monomer and tetracarboxylic dianhydride's monomer, the weight of the inorganic particle Amount percentage is 10wt% to 50wt%.
2. the manufacturing method of polyimide film according to claim 1, which is characterized in that form the polyamic acid mixture The step of further include:
The inorganic particle is dissolved in a solvent and is uniformly mixed and forms a suspension;And
The diamine monomer is added in the suspension to be uniformly mixed to form the polyamic acid mixture with tetracarboxylic dianhydride's monomer.
3. the manufacturing method of polyimide film according to claim 2, which is characterized in that the diamine monomer and the tetrabasic carboxylic acid The molar ratio of dianhydride monomer is 0.98:1 to 1.05:1.
4. the manufacturing method of polyimide film according to claim 1, which is characterized in that the thermal conductivity system of the polyimide film Number is more than or equal to 0.4W/mK.
5. the manufacturing method of polyimide film according to claim 4, which is characterized in that the thermal conductivity system of the polyimide film Number is 0.45W/mK to 0.75W/mK.
6. the manufacturing method of polyimide film according to claim 1, which is characterized in that the inorganic particle is selected from oxidation Aluminium, boron nitride, zinc oxide, aluminium nitride, barium titanate and its group formed.
7. the manufacturing method of polyimide film according to claim 2, which is characterized in that the solvent is selected from dimethyl formyl Amine, dimethyl acetamide, dimethyl sulfoxide (DMSO), n-methyl-2-pyrrolidone and its group formed.
8. the manufacturing method of polyimide film according to claim 1, which is characterized in that the diamine monomer is selected to benzene two Amine, m-phenylene diamine (MPD), 4,4'- diaminodiphenyl ethers, 3,4'- diaminodiphenyl ethers, 4,4'- diamino hexichol alkane, DPD di p phenylenediamine, Diamino benzophenone, diamines diphenyl sulfone, two naphthylenediamines, diaminodiphenyl sulfide, 1,3- double (3- amino phenols oxygroup) benzene, 1,4- Double (the 4- amino phenols oxygroup) benzene of double (4- amino phenols oxygroup) benzene, 1,3-, 2,2- double [4- (4- amino phenols oxygroup) phenyl] propane, 4, Double (the 4- amino phenols oxygroup) biphenyl of 4'-, 4,4'- double (3- amino phenols oxygroup) biphenyl, 1,3- dipropyl amido -1,1', 3,3'- tetramethyls Base disiloxane, 1,3- dipropyl amido -1,1', 3,3'- tetraphenyls disiloxane, 1,3- dipropyl amido -1,1- dimethyl -3,3- Diphenyl disiloxane and its group formed.
9. the manufacturing method of polyimide film according to claim 1, which is characterized in that tetracarboxylic dianhydride's monomer is selected from Pyromellitic acid anhydride, biphenyl tetracarboxylic dianhydride, oxydiphthalic, benzophenone tetracarboxylic dianhydride, diphenyl sulfone tetrabasic carboxylic acid Double (the 3,4- dicarboxyl benzene of dianhydride, naphthalene tetracarboxylic dianhydride, naphthalene dicarboxylic anhydride, double-(3,4- phthalate anhydrides) dimethylsilane, 1,3- Base) -1,1', 3,3'- tetramethyl disiloxanes dianhydride and its group formed.
10. the manufacturing method of polyimide film according to claim 1, which is characterized in that the drying temperature for 120 DEG C extremely 200℃。
11. the manufacturing method of polyimide film according to claim 1, which is characterized in that the weight hundred of the inorganic particle Divide than being 20wt% to 35wt%.
12. the manufacturing method of polyimide film according to claim 1, which is characterized in that the weight hundred of the inorganic particle Divide than being 23wt% to 31.5wt%.
13. the manufacturing method of the polyimide film according to claim 1 to 12 any of which item, which is characterized in that by this Polyamide acid film carries out the step of Asia amidation process forms the polyimide film and in the polyamide acid film single shaft is subject to prolong The Asia amidation process is carried out under the situation stretched.
14. the manufacturing method of polyimide film according to claim 13, which is characterized in that carried out to the polyamide acid film One uniaxial tension tension of the uniaxial extension is 0.05MPa to 0.5MPa.
15. the manufacturing method of polyimide film according to claim 13, which is characterized in that carried out to the polyamide acid film One uniaxial tension tension of the uniaxial extension is 0.1MPa.
16. a kind of polyimide film, which is characterized in that it utilizes the polyamides according to claim 1 to 15 any of which item Obtained by the manufacturing method of imines film.
CN201710535303.7A 2016-11-30 2017-07-04 Method for producing polyimide film, and polyimide film Pending CN108117655A (en)

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