WO2022228449A1 - Preparation method for polyimide resin and thin film thereof - Google Patents

Preparation method for polyimide resin and thin film thereof Download PDF

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WO2022228449A1
WO2022228449A1 PCT/CN2022/089436 CN2022089436W WO2022228449A1 WO 2022228449 A1 WO2022228449 A1 WO 2022228449A1 CN 2022089436 W CN2022089436 W CN 2022089436W WO 2022228449 A1 WO2022228449 A1 WO 2022228449A1
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bis
dianhydride
batch
polyimide resin
viscosity
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PCT/CN2022/089436
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French (fr)
Chinese (zh)
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程跃
吴超
吕凯
刘倩倩
庄志
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上海瑞暨新材料科技有限公司
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Publication of WO2022228449A1 publication Critical patent/WO2022228449A1/en

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    • 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
    • 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
    • C08G73/1003Preparatory processes
    • C08G73/1007Preparatory processes from tetracarboxylic acids or derivatives and diamines
    • 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
    • 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

Definitions

  • the present disclosure relates to the field of polyimide films, in particular to a preparation method of polyimide resin and a film thereof.
  • polyamic acid is synthesized by low-temperature polycondensation by first diamine and then dianhydride in an equimolar amount in a suitable organic solvent, and then by casting a film on the substrate, and finally thermal imidization to form a film.
  • this preparation method makes the polymer It is difficult to control the apparent viscosity of amic acid within an ideal range of higher viscosity, the length of polymer molecular segments is not balanced, the resin viscosity is difficult to stabilize, and the amount of resin bubbles is large, and the experimental process found that when the dianhydride and diamine are close When the molar ratio is equal, the viscosity will show a similar exponential jump.
  • the present disclosure provides a preparation method of polyimide with stable performance and viscosity under long-term storage, which specifically includes the following steps:
  • the low temperature environment in step S1 is -20-30°C.
  • the added amount of the second batch of polyvalent diamines in step S2 is 5-10% of the total molar amount of the first batch of polyvalent diamines
  • the specific operation of batch addition is: adding in a temperature gradient of 30-35 °C 40% of the total molar amount of the second batch of polyvalent diamines, adding 25% of the total molar amount of the second batch of polyvalent diamines in a temperature gradient of 45-50 °C, adding the second batch of polyvalent diamines in a temperature gradient of 65-70 °C Add 20% of the total amount of polydiamine in the 75-80 °C temperature gradient, add 10% of the total molar amount of the second batch of polydiamine, continue to stir and monitor the viscosity of the resin solution, if the resin viscosity is stable at 180000-200000cps, then stop feeding, otherwise, then Continue adding the remaining second batch of polydiamine until the resin viscosity stabilizes at 50,000-70,000 cps.
  • the total molar amount of the fluorine-containing capping agent plus the molar amount of the first batch of polybasic diamine and the second batch of polyvalent diamine is approximately equal to the molar amount of polybasic dianhydride.
  • the polydiamines include p-phenylenediamine and its ring fluorinated compounds, benzidine and its ring fluorinated compounds, 4,4'-oxydiphenylamine, 1,3-bis( 4-Aminophenoxy)benzene, 1,3-bis(3-aminophenoxy)benzene, 1,3-bis(2-aminophenoxy)benzene, 4,4'-bis(3-aminobenzene) oxy) biphenyl, 4,4'-bis(4-aminophenoxy)biphenyl, 4,4'-bis(5-aminophenoxy)biphenyl, bis(4-(4-aminophenoxy) base)phenyl)sulfone, bis(4-(3-aminophenoxy)phenyl)sulfone, bis(4-(2-aminophenoxy)phenyl)sulfone, 4,4'-diaminodiphenyl Ethane, 4,4'-
  • the polybasic dianhydride includes pyromellitic dianhydride, 2,3,6,7-tetracarboxylic dianhydride, 3,3',4,4'-biphenyltetracarboxylic dianhydride Anhydride, 1,2,5,6-naphthalenetetracarboxylic dianhydride, 2,2',3,3'-biphenyltetracarboxylic dianhydride, 2,2-bis(3,4-dicarboxyphenyl) Propane dianhydride, 3,4,9,10-tetracarboxylic dianhydride, bis(3,4-dicarboxyphenyl)propane dianhydride, 1,1-bis(2,3-dicarboxyphenyl)ethane Dianhydride, 1,1-bis(3,4-dicarboxyphenyl)ethane dianhydride, bis(2,3-dicarboxyphenyl)methane dianhydride, bis(3,4-dicarbox
  • the fluorine-containing capping agent includes a fluorine-containing monoamine aromatic organic compound.
  • the fluorine-containing capping agent includes m-bis(trifluoromethyl)aniline, 4-(4'-fluorophenyl)benzonitrile, p-trifluoromethylaniline, 2,6-difluoromethylaniline Fluoro-3-methylaniline, cyanoacetyl-p-trifluoromethylaniline, 4-methyl-2-(trifluoromethyl)aniline, 3-fluoro-2-(trifluoromethyl)aniline, 5-fluoro -2-trifluoromethylaniline, 4-fluoro-2-nitro-5-(trifluoromethyl)-aniline, 2,2'-bis(trifluoromethyl)diaminobiphenyl, trifluoroaniline, N-ethyl-2,3,5-trifluoroaniline, 2,2'-bis(3,4,5-trifluorophenyl)-4,4'-benzidinediamine, 2,3,4- Any of trifluorophenylacetamide and 2,3,4-trifluorophen
  • the solvent includes N,N-dimethylformamide, N,N-dimethylacetamide, N-methylpyrrolidone, cyclohexane, methylcyclohexane, tetrahydrofuran, isohexane , n-heptane, dichloromethane, trichloroethylene, carbon tetrachloride, epichlorohydrin, methyl methacrylate, dimethyl sulfoxide.
  • the present disclosure also provides the polyimide resin prepared by the above-mentioned preparation method.
  • the present disclosure also provides the use of the polyimide resin in a film.
  • the present disclosure also provides a film, the preparation method comprising: selecting the above-mentioned polyimide resin, sequentially adding a catalyst and a dehydrating agent to the polyimide resin, and coating the film on at least one side of the base film.
  • the catalyst includes pyridazine, pyrimidine, pyridine, phthalazine, 1,10-phenanthroline.
  • the mass ratio of the catalyst to the polyimide resin solution is 1:95-105.
  • the base film includes carbon nanofiber copper foil, carbon nanofiber silver foil, carbon nanofiber aluminum foil, and carbon nanofiber gold foil.
  • the present disclosure provides a preparation method of a polyimide resin, comprising the following steps:
  • the first batch of polybasic diamine and polybasic dianhydride are firstly polymerized into a low-viscosity resin solution at a low temperature, and then gradually heated at 30-80°C.
  • the present disclosure emphasizes the second The batch of polyvalent diamines is added to the resin solution gradually by the differential method in different temperature gradients, so that the polymer segments are continuously reformed, homogenized and then lengthened. When the lengths of all segments are kept balanced, the chain
  • the polyimide resin solution prepared by this preparation method is homogeneous and stable, as shown in Table 1. Compared with the polyimide resin solution prepared by the current technology, it can last for a long time.
  • the polyimide resin solution can be stored for a long time; at the same time, the fluorine-containing end-capping agent can effectively reduce the hydrolysis of the end chain of the polyimide resin solution, and further improve the viscosity stability of the polyimide resin solution.
  • the structure of the film is more stable, the tensile strength of the film will be enhanced accordingly, and the fluorine-containing compound also has the effect of reducing the dielectric constant. leakage, heat generation and capacitance effects between wires.
  • the monitoring method of the above-mentioned monitoring resin is not limited to any method that can grasp the viscosity of the polyimide resin at any time.
  • the total molar amount of the first batch of polyvalent diamines and the second batch of polyvalent diamines in the present disclosure is similar to the total molar amount of polyvalent dianhydrides.
  • the ratio of the total molar amount of the first batch of polyvalent diamine and the second batch of polyvalent diamine to the total molar amount of polyvalent dianhydride is 0.9-1.0:1.0 , for example, 0.92-1.0:1.0, 0.92-0.98:1.0, or 0.94-0.96:1.0.
  • the low temperature environment in the step S1 of the present disclosure is -20-30°C.
  • the reaction is a reaction that increases the exothermic entropy, so the low temperature helps the molecular chain segment
  • the polymerization reaction promotes the reaction to proceed in the forward direction, so that the molecular segments continue to grow and the viscosity increases. Therefore, in some typical embodiments, the low temperature environment can be -20-10°C, -10-0°C, 0- 10°C, 10-30°C.
  • the second batch of polyvalent diamines is added in batches in the S2 step in batches.
  • the second batch of polyvalent diamines is added in an amount of 5-10% of the molar total amount of the first batch of polyvalent diamines, such as 6-9 %, 6-8% or 7-8%, added in batches
  • the specific operation is: 30-35 °C (such as 31-35 °C, 31-34 °C or 32-33 °C) temperature gradient adding the second batch of polydiamine 40% of the total molar amount, 25% of the total molar amount of the second batch of polydiamines was added within a temperature gradient of 45-50°C (such as 46-50°C, 46-48°C or 46-47°C), 65-70°C ( Add 20% of the total molar amount of the second batch of polydiamine within a temperature gradient such as 66-69°C, 66-68°C or 66-67°C, 75-80°C (such as 76-79°C,
  • the total molar amount of the fluorine-containing end-capping agent plus the first batch of polyvalent diamine and the second batch of polyvalent diamine can be further limited to be approximately equal to the molar amount of polyvalent dianhydride.
  • thermo expansion coefficient of the prepared polyimide resin solution after film formation can be equal to that of the base film, so as to avoid the phenomenon of curling at the edge of the film due to a large difference in the expansion coefficient.
  • n ⁇ 2 as shown in Table 1, under the same polybasic diamine and polybasic dianhydride, by changing the ratio between polybasic diamines and the ratio between polybasic dianhydrides Mixing ratios can obtain polyimide films with different thermal expansion coefficients.
  • the present disclosure has no special restrictions on the diamine, which can be any well-known diamine in the art, specifically, p-phenylenediamine and its ring fluorinated compound, benzidine and its ring fluorinated compound, 4, 4'-Oxydiphenylamine, 1,3-bis(4-aminophenoxy)benzene, 1,3-bis(3-aminophenoxy)benzene, 1,3-bis(2-aminophenoxy) ) benzene, 4,4'-bis(3-aminophenoxy)biphenyl, 4,4'-bis(4-aminophenoxy)biphenyl, 4,4'-bis(5-aminophenoxy) ) biphenyl, bis(4-(4-aminophenoxy)phenyl)sulfone, bis(4-(3-aminophenoxy)phenyl)sulfone, bis(4-(2-aminophenoxy) phenyl) sulfone
  • dianhydride in the present disclosure, can be any dianhydride known in the art, and specific examples include pyromellitic dianhydride, 2,3,6,7-tetracarboxylic dianhydride, 3,3' ,4,4'-biphenyltetracarboxylic dianhydride, 1,2,5,6-naphthalenetetracarboxylic dianhydride, 2,2',3,3'-biphenyltetracarboxylic dianhydride, 2,2 -Bis(3,4-dicarboxyphenyl)propane dianhydride, 3,4,9,10-tetracarboxylic dianhydride, bis(3,4-dicarboxyphenyl)propane dianhydride, 1,1-bis (2,3-Dicarboxyphenyl)ethanedianhydride, 1,1-bis(3,4-dicarboxyphenyl)ethanedianhydride, bis(2,3-dicarboxy
  • the fluorine-containing end-capping agent of the present disclosure is a fluorine-containing monoamine aromatic organic compound, which reacts with the end-chain anhydride structure of the polyimide resin solution to perform end-chain end-capping, so that the end-chain structure of the polyimide resin solution is
  • the amino structure of the fluorine-containing end-capping agent so as to avoid the hydrolysis of the polyimide resin solution, the fluorine-containing end-capping agent can be listed as m-bis(trifluoromethyl)aniline, 4-(4'-fluorophenyl)benzyl Nitrile, p-trifluoromethylaniline, 2,6-difluoro-3-methylaniline, cyanoacetyl p-trifluoromethylaniline, 4-methyl-2-(trifluoromethyl)aniline, 3-fluoro -2-(trifluoromethyl)aniline, 5-fluoro-2-trifluoromethylaniline, 4-fluoro-2-nitro-5-(trifluor
  • solvents which can be listed as N,N-dimethylformamide, N,N-dimethylacetamide, N-methylpyrrolidone, cyclohexane, methylcyclohexane, tetrahydrofuran , isohexane, n-heptane, dichloromethane, trichloroethylene, carbon tetrachloride, epichlorohydrin, methyl methacrylate, dimethyl sulfoxide.
  • solvents which can be listed as N,N-dimethylformamide, N,N-dimethylacetamide, N-methylpyrrolidone, cyclohexane, methylcyclohexane, tetrahydrofuran , isohexane, n-heptane, dichloromethane, trichloroethylene, carbon tetrachloride, epichlorohydrin, methyl methacrylate, dimethyl sulfoxide.
  • a catalyst and a dehydrating agent are sequentially added to the solution to rapidly dehydrate and imidize the polyimide acid to form a film, so as to improve the production efficiency.
  • the tensile strength of the film is increased.
  • the present disclosure also expands the catalyst types that are not currently used in the art.
  • the catalyst can be a monocyclic or condensed ring compound, such as pyridazine, pyrimidine, pyridine, phthalazine
  • 1,10-phenanthroline as shown in Table 1, when the catalyst emphasized in this disclosure is selected, a polyimide film with more excellent tensile strength can be obtained.
  • a combination of pyridazine and pyridine can be selected. The catalytic performance is the best, and the mass ratio of the two catalysts is 1:4.
  • the optimal ratio of the controllable catalyst and the polyimide resin solution is to control the mass ratio of the two within the range of 1:95-105.
  • the above-mentioned base films are not particularly limited, and can be base films commonly used in the field, such as carbon nanofiber copper foil, carbon nanofiber silver foil, carbon nanofiber aluminum foil, carbon nanofiber gold foil, but due to the excellent heat dissipation performance of carbon nanofiber copper foil , high strength, extremely stable chemical properties, low price and other characteristics can solve the problem of heat dissipation and oxidation of circuit boards, and save costs, so in some typical embodiments, the base film can be carbon nanofiber copper foil.
  • the preparation method provided by the present disclosure can make the polyimide stable in performance and viscosity under long-term storage.
  • the preparation method of the present disclosure solves the problems of viscosity control and viscosity stability.
  • the polyimide resin obtained by the preparation method is uniform and stable, and can be stored in a natural environment at normal temperature and pressure for a long time without changing the viscosity and performance;
  • the end agent solves the problem that the acid anhydride of the end chain is easy to be hydrolyzed.
  • the end chain is capped by adding a suitable molar ratio of monoamine aromatic organic compounds.
  • the end chain structure is an amino structure, which completely avoids the problem of the end group being hydrolyzed.
  • the problem of high dielectric constant of imine resins is because fluorine-containing compounds have the effect of reducing the dielectric constant. Therefore, by adding an appropriate amount of fluorine-containing amine organic compounds, the dielectric constant can be effectively reduced, thereby reducing the leakage, heat generation of integrated circuits and between wires. capacitive effect.
  • the formed polyimide coating has strong thermal stability, and the thermal expansion coefficient is close to that of the base film.
  • the film edge is prone to curling.
  • the prepared mixed solution adopts the principle of adding more first and then less multiple times, adding 40% at 30°C-35°C, adding 25% at 45°C-50°C, adding 20% at 65°C-70°C, and adding at 75°C-80°C 10%, the remaining part is added at a temperature of 80 °C and stirred for 1 hour, depending on the viscosity.
  • the stirring rate is 15rad/min.
  • the water bath was heated to 80°C, and 0.00438mol p-phenylenediamine and 0.00438mol 4,4'-diphenyletherdiamine were weighed and dissolved in 4g N,N-dimethylformamide under nitrogen atmosphere.
  • the difference method is used to add more first and then less. Add 40% at 30°C-35°C, 25% at 45°C-50°C, 20% at 65°C-70°C, and 10% at 75°C-80°C. %, the remaining part is added at a temperature of 80 °C and stirred for 1 hour depending on the viscosity.
  • the stirring rate is 15rad/min.
  • Fluoromethyl)aniline fully reacted for 60min, cooled to room temperature, weighed 107.57g N,N-dimethylformamide to gradually dilute the resin viscosity to 50000cP, took 100g of the diluted resin, added 0.2g pyridazine and 0.8g g pyridine, stir at a constant speed for 5 min, and then rapidly defoam in high vacuum.
  • Coat the glass substrate and carbon nanofiber copper foil by casting method (the thickness of the film is controlled at about 20 ⁇ m).
  • the acetic anhydride and solvent were removed in a vacuum oven. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
  • the water bath was heated to 80°C, and 0.00500mol p-phenylenediamine and 0.00333mol 4,4'-diphenyletherdiamine were weighed and dissolved in 4g N,N-dimethylformamide under nitrogen atmosphere.
  • the difference method is used to add more first and then less. Add 40% at 30°C-35°C, 25% at 45°C-50°C, 20% at 65°C-70°C, and 10% at 75°C-80°C. %, the remaining part is added at a temperature of 80 °C and stirred for 1 hour depending on the viscosity.
  • the stirring rate is 15rad/min.
  • Fluoromethyl)aniline fully reacted for 60min, cooled to room temperature, weighed 166.37g N,N-dimethylformamide to gradually dilute the resin viscosity to 50000cP, took 100g of the diluted resin, added 0.2g pyridazine and 0.8g Pyridine, stirred at a constant speed for 5 minutes, then rapidly degassed in high vacuum, and coated on glass substrate and carbon nanofiber copper foil by casting method (film thickness was controlled at about 20 ⁇ m), and after chemical imidization, oxygen-free vacuum at 250 °C was used. The oven removes acetic anhydride and solvent. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
  • the water bath was heated to 80°C, and 0.00334mol p-phenylenediamine and 0.00500mol 4,4'-diphenyletherdiamine were weighed and dissolved in 4g N,N-dimethylformamide under nitrogen atmosphere.
  • the difference method is used to add more first and then less. Add 40% at 30°C-35°C, 25% at 45°C-50°C, 20% at 65°C-70°C, and 10% at 75°C-80°C. %, the remaining part is added at a temperature of 80 °C and stirred for 1 hour depending on the viscosity.
  • the stirring rate is 15 rad/min.
  • Fluoromethyl)aniline fully reacted for 60min, cooled to room temperature, weighed 106.95g N,N-dimethylformamide to gradually dilute the resin viscosity to 50000cP, took 100g of the diluted resin, added 0.2g pyridazine and 0.8g Pyridine, stirred at a constant speed for 5 minutes, then rapidly degassed in high vacuum, and coated on glass substrate and carbon nanofiber copper foil by casting method (film thickness was controlled at about 20 ⁇ m), and after chemical imidization, oxygen-free vacuum at 250 °C was used. The oven removes acetic anhydride and solvent. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is checked after one month.
  • the water bath was heated to 80°C, and 0.00375mol p-phenylenediamine and 0.00250mol 4,4'-diphenyletherdiamine were weighed and dissolved in 4g N,N-dimethylformamide under nitrogen atmosphere.
  • the difference method is used to add more first and then less. Add 40% at 30°C-35°C, 25% at 45°C-50°C, 20% at 65°C-70°C, and 10% at 75°C-80°C. %, the remaining part is added at a temperature of 80 °C and stirred for 1 hour, depending on the viscosity.
  • the stirring rate is 15rad/min.
  • Fluoromethyl)aniline fully reacted for 60min, cooled to room temperature, weighed 127.25g N,N-dimethylformamide to gradually dilute the resin viscosity to 50000cP, took 100g of the diluted resin, added 0.2g pyridazine and 0.8g Pyridine, stirred at a constant speed for 5 minutes, then rapidly degassed in high vacuum, and coated on glass substrate and carbon nanofiber copper foil by casting method (film thickness was controlled at about 20 ⁇ m), and after chemical imidization, oxygen-free vacuum at 250 °C was used. The oven removes acetic anhydride and solvent. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
  • the film is coated on the glass substrate (the thickness of the film is controlled at about 20 ⁇ m), and the film is formed by imidization in an oxygen-free vacuum oven at 500 °C. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
  • the film is coated on the glass substrate (the thickness of the film is controlled at about 20 ⁇ m), and the film is formed by imidization in an oxygen-free vacuum oven at 500 °C. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
  • the film is coated on the glass substrate (the thickness of the film is controlled at about 20 ⁇ m), and the film is formed by imidization in an oxygen-free vacuum oven at 500 °C. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
  • the film is coated on the glass substrate (the thickness of the film is controlled at about 20 ⁇ m), and the film is formed by imidization in an oxygen-free vacuum oven at 500 °C. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
  • the film is coated on the glass substrate (the thickness of the film is controlled at about 20 ⁇ m), and the film is formed by imidization in an oxygen-free vacuum oven at 500 °C. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
  • the films prepared in Comparative Examples 1-5 have low tensile strength, large difference in thermal expansion coefficient and copper foil, high water absorption, high dielectric constant, and obvious curling phenomenon of the film, which cannot meet the requirements of industrial production.
  • the tensile strength was greater than 120MPa
  • the thermal expansion coefficient was close to that of copper foil (18 ⁇ 10-6k-1)
  • the water absorption rate was low, all less than 2%
  • the dielectric constant is less than 3
  • the film does not produce curling phenomenon, indicating that the performance is good
  • the graphene copper foil is used as the base film
  • the tensile strength of the prepared film is greatly increased by more than 320MPa
  • the thermal expansion coefficient is close to that of copper foil ( 18 ⁇ 10-6k-1)
  • the water absorption rate is low, less than 2%
  • the dielectric constant is less than 3
  • the outer side of the film has a very small curling phenomenon, indicating that the performance is good and
  • the present disclosure provides a method for preparing polyimide resin and a film thereof.
  • the polyimide prepared in the present disclosure has the characteristics of long-term storage performance and stable viscosity, and the polyimide resin prepared in the present disclosure is coated on
  • the formed polyimide coating has strong thermal stability, and the thermal expansion coefficient is close to the base film, which solves the problem that the edge of the film is easily curled due to the large difference in the thermal expansion coefficient. Therefore, the polyimide prepared by the present disclosure and the film prepared therefrom have excellent industrial practical properties and good market prospects.

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Abstract

The present disclosure relates to the field of polyimide, and in particular to a preparation method for a polyimide resin and a thin film thereof. The method comprises the following steps: S1, upon dissolving a first batch of polydiamine in a solvent under an inert gas atmosphere, adding polydianhydride in a low-temperature environment of 30°C or below for preliminary polymerization to form a resin solution, wherein the polydianhydride is 105-110% of the total molar amount of the first batch of polydiamine and the viscosity of the resin solution is controlled to be 50,000-70,000 cps; S2, monitoring the viscosity of the resin solution and gradually raising the temperature of the resin solution within 30-80°C, and gradually adding a second batch of polyamine in batches in order of descending amounts until the viscosity of the resin solution is 180,000-200,000 cps; and S3, adding a fluorine-containing capping agent, performing uniform mixing, and performing high-vacuum defoaming to obtain a polyimide resin solution. When the polyimide resin prepared in the present disclosure is coated on a base film to prepare a thin film, a formed polyimide coating has strong thermal stability a coefficient of thermal expansion close to that of the base film, and the problem that the edge of the thin film generated in the case of a relatively large difference in coefficients of thermal expansion is prone to curl and shrink is solved.

Description

一种聚酰亚胺树脂的制备方法及其薄膜A kind of preparation method of polyimide resin and film thereof
相关申请的交叉引用CROSS-REFERENCE TO RELATED APPLICATIONS
本公开要求于2021年04月29日提交中国专利局的申请号为“CN 202110474312.6”名称为“一种聚酰亚胺树脂的制备方法及其薄膜”的中国专利申请的优先权,其全部内容通过引用结合在本公开中。This disclosure claims the priority of the Chinese patent application with the application number "CN 202110474312.6" and the title "A preparation method of polyimide resin and film thereof" filed with the China Patent Office on April 29, 2021, the entire contents of which are Incorporated in this disclosure by reference.
技术领域technical field
本公开涉及聚酰亚胺薄膜领域,具体是一种聚酰亚胺树脂的制备方法及其薄膜。The present disclosure relates to the field of polyimide films, in particular to a preparation method of polyimide resin and a film thereof.
背景技术Background technique
目前多采用在适宜的有机溶剂中先二胺后二酐等摩尔投入进行低温缩聚反应合成聚酰胺酸,然后通过在基板流延涂膜,最后热亚胺化成膜,但该制备方法使得聚酰胺酸表观粘度较难控制在一个粘度较大理想需求范围,聚合物分子链段长短不均衡,树脂粘度难以稳定,树脂气泡量较大,且实验过程发现当二酐与二胺两者接近等摩尔比时粘度会呈现类似指数型跳跃,因此常规加料方式在低温环境聚合控制树脂表观粘度就比较困难,往往会出现加入极微量的二酐粘度激增远超预期范围,或者常温下短期粘度下降显著的情况,给工业批量生产带来巨大的困难,直接添加二胺固体控制粘度又容易出现局部高度团聚难缩聚的现象,降低聚酰亚胺树脂的性能品质,由此制备的薄膜性能亦不优异。At present, polyamic acid is synthesized by low-temperature polycondensation by first diamine and then dianhydride in an equimolar amount in a suitable organic solvent, and then by casting a film on the substrate, and finally thermal imidization to form a film. However, this preparation method makes the polymer It is difficult to control the apparent viscosity of amic acid within an ideal range of higher viscosity, the length of polymer molecular segments is not balanced, the resin viscosity is difficult to stabilize, and the amount of resin bubbles is large, and the experimental process found that when the dianhydride and diamine are close When the molar ratio is equal, the viscosity will show a similar exponential jump. Therefore, it is difficult to control the apparent viscosity of the resin by polymerization in a low temperature environment with conventional feeding methods. It is often seen that a very small amount of dianhydride is added. The viscosity surges far beyond the expected range, or the short-term viscosity at room temperature The situation of significant decline brings huge difficulties to industrial mass production. Directly adding diamine solid to control the viscosity is prone to the phenomenon of local high agglomeration and difficult polycondensation, which reduces the performance quality of polyimide resin. Not excellent.
发明内容SUMMARY OF THE INVENTION
本公开提供一种长期存储下性能、粘度均稳定的聚酰亚胺的制备方法,具体包括以下步骤:The present disclosure provides a preparation method of polyimide with stable performance and viscosity under long-term storage, which specifically includes the following steps:
S1、将第一批多元二胺在惰性气体氛围下溶解于溶剂中后,在30℃及以下的低温环境中加入105-110%第一批多元二胺摩尔总量的多元二酐先行聚合形成树脂溶液,控制树脂溶液粘度在50000-70000cps;S1. After dissolving the first batch of polyvalent diamines in a solvent under an inert gas atmosphere, add 105-110% of the first batch of polyvalent diamines in a low-temperature environment of 30 ° C and below, and then polymerize to form Resin solution, control the viscosity of resin solution at 50000-70000cps;
S2、监控树脂溶液粘度并在30-80℃内逐步升温,将第二批多元二胺分批量先多后少逐步加入,直至树脂溶液粘度为180000-200000cps;S2. Monitor the viscosity of the resin solution and gradually increase the temperature within 30-80°C, and gradually add the second batch of polybasic diamines in batches, until the viscosity of the resin solution is 180000-200000cps;
S3、加入含氟封端剂混合,高真空消泡后得到聚酰亚胺树脂溶液。S3, adding a fluorine-containing end-capping agent and mixing, and obtaining a polyimide resin solution after high-vacuum defoaming.
在一些实施方式中,S1步骤中的低温环境为-20-30℃。In some embodiments, the low temperature environment in step S1 is -20-30°C.
在一些实施方式中,S2步骤中所述第二批多元二胺加入量为第一批多元二胺摩尔总量的5-10%,分批量加入具体操作为:30-35℃温度梯度内添加第二批多元二胺摩尔总量的40%,45-50℃温度梯度内添加第二批多元二胺摩尔总量的25%,65-70℃温度梯度内添加第二批多元二胺摩尔总量的20%,75-80℃温度梯度内添加第二批多元二胺摩尔总量的10%,持续搅拌并监测树脂溶液粘度,若树脂粘度稳定在180000-200000cps,则停止加料,反之,则继续添加剩余第二批多元二胺直至树脂粘度稳定在50000-70000cps。In some embodiments, the added amount of the second batch of polyvalent diamines in step S2 is 5-10% of the total molar amount of the first batch of polyvalent diamines, and the specific operation of batch addition is: adding in a temperature gradient of 30-35 °C 40% of the total molar amount of the second batch of polyvalent diamines, adding 25% of the total molar amount of the second batch of polyvalent diamines in a temperature gradient of 45-50 °C, adding the second batch of polyvalent diamines in a temperature gradient of 65-70 °C Add 20% of the total amount of polydiamine in the 75-80 °C temperature gradient, add 10% of the total molar amount of the second batch of polydiamine, continue to stir and monitor the viscosity of the resin solution, if the resin viscosity is stable at 180000-200000cps, then stop feeding, otherwise, then Continue adding the remaining second batch of polydiamine until the resin viscosity stabilizes at 50,000-70,000 cps.
在一些实施方式中,含氟封端剂摩尔总量加上第一批多元二胺、第二批多元二胺摩尔量约等于多元二酐摩尔量。In some embodiments, the total molar amount of the fluorine-containing capping agent plus the molar amount of the first batch of polybasic diamine and the second batch of polyvalent diamine is approximately equal to the molar amount of polybasic dianhydride.
在一些实施方式中,所述多元二胺包括对苯二胺及其环上氟代化合物、联苯胺及其环上氟代化合物、4,4'-氧基二苯胺、1,3-双(4-氨基苯氧基)苯、1,3-双(3-氨基苯氧基)苯、1,3-双(2-氨基苯氧基)苯、4,4'-双(3-氨基苯氧基)联苯、4,4'-双(4-氨基苯氧基)联苯、4,4'-双(5-氨基苯氧基)联苯、双(4-(4-氨基苯氧基)苯基)砜、双(4-(3-氨基苯氧基)苯基)砜、双(4-(2-氨基苯氧基)苯基)砜、4,4'-二氨基二苯基乙烷、4,4'-二氨基二苯基异丙烷、4,4'-二氨基苯硫醚、3,3'-二氨基二苯砜、4,4'-二氨基二苯砜、3,3'-氧基二苯胺、3,4'-氧基二苯胺、2,4'-氧基二苯胺、4,4'-二氨基二苯基二乙基硅烷、4,4'-二氨基二苯基硅烷、4,4'-二氨基二苯基乙基氧膦、4,4'-二氨基二苯基N-甲胺、4,4'-二氨基二苯基N-苯胺、1,3-二氨基苯、1,2-二氨基苯、2,2'-双[4-(4-氨基苯氧基)苯基]丙烷、2,2'-双[4-(4-氨基苯氧基)苯基]-1,1,1,3,3,3-六氟丙烷、4,4'-二氨基-2,2'-双三氟甲基联苯的任意两种或多种配比。In some embodiments, the polydiamines include p-phenylenediamine and its ring fluorinated compounds, benzidine and its ring fluorinated compounds, 4,4'-oxydiphenylamine, 1,3-bis( 4-Aminophenoxy)benzene, 1,3-bis(3-aminophenoxy)benzene, 1,3-bis(2-aminophenoxy)benzene, 4,4'-bis(3-aminobenzene) oxy) biphenyl, 4,4'-bis(4-aminophenoxy)biphenyl, 4,4'-bis(5-aminophenoxy)biphenyl, bis(4-(4-aminophenoxy) base)phenyl)sulfone, bis(4-(3-aminophenoxy)phenyl)sulfone, bis(4-(2-aminophenoxy)phenyl)sulfone, 4,4'-diaminodiphenyl Ethane, 4,4'-diaminodiphenylisopropane, 4,4'-diaminophenyl sulfide, 3,3'-diaminodiphenylsulfone, 4,4'-diaminodiphenylsulfone, 3,3'-oxydiphenylamine, 3,4'-oxydiphenylamine, 2,4'-oxydiphenylamine, 4,4'-diaminodiphenyldiethylsilane, 4,4'- Diaminodiphenylsilane, 4,4'-diaminodiphenylethylphosphine oxide, 4,4'-diaminodiphenyl N-methylamine, 4,4'-diaminodiphenyl N-aniline , 1,3-diaminobenzene, 1,2-diaminobenzene, 2,2'-bis[4-(4-aminophenoxy)phenyl]propane, 2,2'-bis[4-(4 -Aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoropropane, any two of 4,4'-diamino-2,2'-bistrifluoromethylbiphenyl or multiple ratios.
在一些实施方式中,所述多元二酐包括均苯四羧酸二酐、2,3,6,7-四羧酸二酐、3,3',4,4'-联苯四羧酸二酐、1,2,5,6-萘四羧酸二酐、2,2',3,3'-联苯四羧酸二酐、2,2-双(3,4-二羧苯基)丙烷二酐、3,4,9,10-四羧酸二酐、双(3,4-二羧苯基)丙烷二酐、1,1-双(2,3-二羧苯基)乙烷二酐、1,1-双(3,4-二羧苯基)乙烷二酐、双(2,3-二羧苯基)甲烷二酐、双(3,4-二羧苯基)乙烷二酐、羟基二邻苯二甲酸二酐、双(3,4-二羧苯基)砜二酐、亚乙基双(偏苯三酸单酯酸酐)、双酚A双(偏苯三酸单酯酸酐)、4,4'-氧双邻苯二甲酸酐、4,4'-硫双邻苯二甲酸酐、3,3',4,4'-二苯酮四酸二酐、4,4'-氧双邻苯二甲酸酐、4,4'-(六氟异亚丙基)二邻苯二甲酸酐中的任意两种或多种配比。In some embodiments, the polybasic dianhydride includes pyromellitic dianhydride, 2,3,6,7-tetracarboxylic dianhydride, 3,3',4,4'-biphenyltetracarboxylic dianhydride Anhydride, 1,2,5,6-naphthalenetetracarboxylic dianhydride, 2,2',3,3'-biphenyltetracarboxylic dianhydride, 2,2-bis(3,4-dicarboxyphenyl) Propane dianhydride, 3,4,9,10-tetracarboxylic dianhydride, bis(3,4-dicarboxyphenyl)propane dianhydride, 1,1-bis(2,3-dicarboxyphenyl)ethane Dianhydride, 1,1-bis(3,4-dicarboxyphenyl)ethane dianhydride, bis(2,3-dicarboxyphenyl)methane dianhydride, bis(3,4-dicarboxyphenyl)ethane Alkane dianhydride, hydroxydiphthalic dianhydride, bis(3,4-dicarboxyphenyl) sulfone dianhydride, ethylene bis(trimellitic acid monoester anhydride), bisphenol A bis(trimellitic acid) acid monoester anhydride), 4,4'-oxydiphthalic anhydride, 4,4'-thiodiphthalic anhydride, 3,3',4,4'-benzophenone tetraacid dianhydride, Any two or more ratios of 4,4'-oxydiphthalic anhydride and 4,4'-(hexafluoroisopropylidene)diphthalic anhydride.
在一些实施方式中,所述含氟封端剂包括含氟的单胺类芳香型有机物。In some embodiments, the fluorine-containing capping agent includes a fluorine-containing monoamine aromatic organic compound.
在一些实施方式中,所述含氟封端剂包括间二(三氟甲基)苯胺、4-(4'-氟苯基)苯甲腈、对三氟甲基苯胺、2,6-二氟-3-甲基苯胺、氰基乙酰对三氟甲基苯胺、4-甲基-2-(三氟甲基)苯胺、3-氟-2-(三氟甲基)苯胺、5-氟-2-三氟甲基苯胺、4-氟-2-硝基-5-(三氟甲基)-苯胺、2,2'-二(三氟甲基)二氨基联苯、三氟苯胺、N-乙基-2,3,5-三氟苯胺、2,2'-二(3,4,5-三氟苯基)-4,4'-联苯二胺、2,3,4-三氟苯乙酰胺、2,3,4-三氟-6-硝基苯胺中的任意一种。In some embodiments, the fluorine-containing capping agent includes m-bis(trifluoromethyl)aniline, 4-(4'-fluorophenyl)benzonitrile, p-trifluoromethylaniline, 2,6-difluoromethylaniline Fluoro-3-methylaniline, cyanoacetyl-p-trifluoromethylaniline, 4-methyl-2-(trifluoromethyl)aniline, 3-fluoro-2-(trifluoromethyl)aniline, 5-fluoro -2-trifluoromethylaniline, 4-fluoro-2-nitro-5-(trifluoromethyl)-aniline, 2,2'-bis(trifluoromethyl)diaminobiphenyl, trifluoroaniline, N-ethyl-2,3,5-trifluoroaniline, 2,2'-bis(3,4,5-trifluorophenyl)-4,4'-benzidinediamine, 2,3,4- Any of trifluorophenylacetamide and 2,3,4-trifluoro-6-nitroaniline.
在一些实施方式中,所述溶剂包括N,N-二甲基甲酰胺、N,N-二甲基乙酰胺、N-甲基吡咯烷酮、环己烷、甲基环己烷、四氢呋喃、异己烷、正庚烷、二氯甲烷、三氯乙烯、四氯化碳、环氧氯丙烷、甲基丙烯酸甲酯、二甲亚砜。In some embodiments, the solvent includes N,N-dimethylformamide, N,N-dimethylacetamide, N-methylpyrrolidone, cyclohexane, methylcyclohexane, tetrahydrofuran, isohexane , n-heptane, dichloromethane, trichloroethylene, carbon tetrachloride, epichlorohydrin, methyl methacrylate, dimethyl sulfoxide.
本公开还提供由上述制备方法制备获得的聚酰亚胺树脂。The present disclosure also provides the polyimide resin prepared by the above-mentioned preparation method.
本公开还提供所述聚酰亚胺树脂在薄膜中的用途。The present disclosure also provides the use of the polyimide resin in a film.
本公开还提供一种薄膜,制备方法包括:选用上述的聚酰亚胺树脂,在聚酰亚胺树脂中依次加入催化剂、脱水剂后涂覆在基膜的至少一侧上。The present disclosure also provides a film, the preparation method comprising: selecting the above-mentioned polyimide resin, sequentially adding a catalyst and a dehydrating agent to the polyimide resin, and coating the film on at least one side of the base film.
在一些实施方式中,所述催化剂包括哒嗪、嘧啶、砒嗪、酞嗪亦、1,10-菲咯啉。In some embodiments, the catalyst includes pyridazine, pyrimidine, pyridine, phthalazine, 1,10-phenanthroline.
在一些实施方式中,所述催化剂与聚酰亚胺树脂溶液质量比为1:95-105。In some embodiments, the mass ratio of the catalyst to the polyimide resin solution is 1:95-105.
在一些实施方式中,所述基膜包括碳纳米纤维铜箔、碳纳米纤维银箔、碳纳米纤维铝箔、碳纳米纤维金箔。In some embodiments, the base film includes carbon nanofiber copper foil, carbon nanofiber silver foil, carbon nanofiber aluminum foil, and carbon nanofiber gold foil.
具体实施方式Detailed ways
在描述之前,应当理解,不应将在说明书和所附权利要求书中使用的术语解释为限于一般的词典含义,而应当根据允许本发明人为了最好的解释而合适地限定术语的原则,基于对应于本公开的技术方面的含义和概念进行解释。因此,在此提出的描述仅是为了说明目的而可选的例子,不是为了限制本公开的范围,因此,应当理解,可以在不背离本公开的精神和范围的情况下作出其它的等价物和修改。Before describing, it is to be understood that terms used in the specification and appended claims should not be construed to be limited to their ordinary dictionary meanings, but should be in accordance with principles that allow the inventor to define terms as appropriate for the best interpretation, The explanation is made based on meanings and concepts corresponding to the technical aspects of the present disclosure. Accordingly, the descriptions set forth herein are optional examples for illustrative purposes only and are not intended to limit the scope of the present disclosure, therefore, it is to be understood that other equivalents and modifications may be made without departing from the spirit and scope of the present disclosure .
基于目前国内制备的聚酰亚胺树脂性能、粘度在常温常压下无法长时间保存的问题,本公开提供一种聚酰亚胺树脂的制备方法,包括以下步骤:Based on the problem that the properties and viscosity of the currently prepared polyimide resin cannot be stored for a long time under normal temperature and pressure, the present disclosure provides a preparation method of a polyimide resin, comprising the following steps:
S1、将第一批多元二胺在惰性气体氛围下溶解于溶剂中后,在30℃及以下的低温环境中加入105-110%第一批多元二胺摩尔总量的多元二酐先行聚合 形成树脂溶液,控制树脂溶液粘度在50000-70000cps;其中,树脂溶液粘度可以在诸如55000-70000cps、55000-65000cps或60000-65000cps;加入诸如105-109%、106-108%或105-106%第一批多元二胺摩尔总量的多元二酐先行聚合形成树脂溶液;S1. After dissolving the first batch of polyvalent diamines in a solvent under an inert gas atmosphere, add 105-110% of the first batch of polyvalent diamines in a low-temperature environment of 30 ° C and below, and then polymerize to form Resin solution, control the viscosity of the resin solution at 50000-70000cps; wherein, the resin solution viscosity can be in such as 55000-70000cps, 55000-65000cps or 60000-65000cps; A batch of polyvalent dianhydrides with a total molar amount of polyvalent diamines is first polymerized to form a resin solution;
S2、监控树脂溶液粘度并在30-80℃内逐步升温,将第二批多元二胺分批量先多后少逐步加入,直至树脂溶液粘度为180000-200000cps;其中,监控树脂溶液粘度在诸如40-80℃、40-70℃或50-65℃的范围内逐步升温;S2. Monitor the viscosity of the resin solution and gradually increase the temperature at 30-80 °C, and gradually add the second batch of polybasic diamines in batches, until the viscosity of the resin solution is 180000-200000cps; Gradually increase the temperature in the range of -80°C, 40-70°C or 50-65°C;
S3、加入含氟封端剂混合均匀,高真空消泡后得到聚酰亚胺树脂溶液。S3, adding a fluorine-containing end-capping agent and mixing evenly, and obtaining a polyimide resin solution after high-vacuum defoaming.
采用先低温将第一批多元二胺与多元二酐聚合成低粘度树脂溶液,再于30-80℃内逐步升温,不同于常规的将多元二胺分批次投料,本公开强调将第二批多元二胺采用差量法在不同温度梯度内逐量增加加入树脂溶液中,让高分子链段不断的重整均化再加长的过程,当所有链段长度保持长度均衡的情况下,链段就不容易再发生重排,以此制备方法制备得到的聚酰亚胺树脂溶液均一稳定,如表1所示,相较于目前技术制备而得的聚酰亚胺树脂溶液,能够长时间保持粘度不变,聚酰亚胺树脂溶液能够长时间保存;同时,含氟封端剂能够有效减少聚酰亚胺树脂溶液端链水解,进一步提高聚酰亚胺树脂溶液粘度稳定性,后续制备的薄膜的结构更加稳定,薄膜拉伸强度也会相应增强,含氟化合物还具有降低介电常数的作用,在聚酰亚胺溶液在后续制备成薄膜,应用在电路板中时,降低集成电路的漏电、发热以及导线间电容效应。The first batch of polybasic diamine and polybasic dianhydride are firstly polymerized into a low-viscosity resin solution at a low temperature, and then gradually heated at 30-80°C. Different from the conventional batch feeding of polybasic diamine, the present disclosure emphasizes the second The batch of polyvalent diamines is added to the resin solution gradually by the differential method in different temperature gradients, so that the polymer segments are continuously reformed, homogenized and then lengthened. When the lengths of all segments are kept balanced, the chain The polyimide resin solution prepared by this preparation method is homogeneous and stable, as shown in Table 1. Compared with the polyimide resin solution prepared by the current technology, it can last for a long time. Keeping the viscosity unchanged, the polyimide resin solution can be stored for a long time; at the same time, the fluorine-containing end-capping agent can effectively reduce the hydrolysis of the end chain of the polyimide resin solution, and further improve the viscosity stability of the polyimide resin solution. The structure of the film is more stable, the tensile strength of the film will be enhanced accordingly, and the fluorine-containing compound also has the effect of reducing the dielectric constant. leakage, heat generation and capacitance effects between wires.
上述监控树脂的监控方法不拘泥于任何可以随时掌握聚酰亚胺树脂的粘度方法,可列举的至少有带有粘度探头的粘度测试系统、多次分段取样瓶外测试等本领域常规手段。The monitoring method of the above-mentioned monitoring resin is not limited to any method that can grasp the viscosity of the polyimide resin at any time. There are at least a viscosity testing system with a viscosity probe, multiple sub-sampling outside the bottle testing and other conventional methods in the art.
本公开第一批多元二胺、第二批多元二胺的摩尔量总量与多元二酐的摩尔量总量相近,第二批多元二胺的添加量以树脂粘度到达180000-200000cps为准,例如树脂粘度到达185000-200000cps、185000-195000cps或185000-190000cps,第一批多元二胺、第二批多元二胺的摩尔量总量与多元二酐的摩尔量总量比为0.9-1.0:1.0,例如为0.92-1.0:1.0、0.92-0.98:1.0或0.94-0.96:1.0。The total molar amount of the first batch of polyvalent diamines and the second batch of polyvalent diamines in the present disclosure is similar to the total molar amount of polyvalent dianhydrides. For example, when the resin viscosity reaches 185000-200000cps, 185000-195000cps or 185000-190000cps, the ratio of the total molar amount of the first batch of polyvalent diamine and the second batch of polyvalent diamine to the total molar amount of polyvalent dianhydride is 0.9-1.0:1.0 , for example, 0.92-1.0:1.0, 0.92-0.98:1.0, or 0.94-0.96:1.0.
本公开S1步骤中的低温环境为-20-30℃,在多元二胺与多元二酐初步聚合形成树脂溶液时,该反应为放热熵增大的一个反应,因此低温有助于分子 链段的聚合反应,促使了反应朝正向进行,使得分子链段不断增长,粘度升高,因此在一些典型的实施方式中,低温环境可以为-20-10℃、-10-0℃、0-10℃、10-30℃。The low temperature environment in the step S1 of the present disclosure is -20-30°C. When the polybasic diamine and polybasic dianhydride are preliminarily polymerized to form a resin solution, the reaction is a reaction that increases the exothermic entropy, so the low temperature helps the molecular chain segment The polymerization reaction promotes the reaction to proceed in the forward direction, so that the molecular segments continue to grow and the viscosity increases. Therefore, in some typical embodiments, the low temperature environment can be -20-10°C, -10-0°C, 0- 10°C, 10-30°C.
做为S2步骤中第二批多元二胺分批量加入的具体操作方法,S2步骤中第二批多元二胺加入量为第一批多元二胺摩尔总量的5-10%,诸如6-9%、6-8%或7-8%,分批量加入具体操作为:30-35℃(诸如31-35℃、31-34℃或32-33℃)温度梯度内添加第二批多元二胺摩尔总量的40%,45-50℃(诸如46-50℃、46-48℃或46-47℃)温度梯度内添加第二批多元二胺摩尔总量的25%,65-70℃(诸如66-69℃、66-68℃或66-67℃)温度梯度内添加第二批多元二胺摩尔总量的20%,75-80℃(诸如76-79℃、76-78℃或76-77℃)温度梯度内添加第二批多元二胺摩尔总量的10%,持续搅拌并监测树脂溶液粘度,若树脂粘度稳定在指定数值范围内,则停止加料,反之,则继续添加剩余第二批多元二胺直至树脂粘度达到指定数值。As the concrete operation method that the second batch of polyvalent diamines is added in batches in the S2 step, in the S2 step, the second batch of polyvalent diamines is added in an amount of 5-10% of the molar total amount of the first batch of polyvalent diamines, such as 6-9 %, 6-8% or 7-8%, added in batches The specific operation is: 30-35 ℃ (such as 31-35 ℃, 31-34 ℃ or 32-33 ℃) temperature gradient adding the second batch of polydiamine 40% of the total molar amount, 25% of the total molar amount of the second batch of polydiamines was added within a temperature gradient of 45-50°C (such as 46-50°C, 46-48°C or 46-47°C), 65-70°C ( Add 20% of the total molar amount of the second batch of polydiamine within a temperature gradient such as 66-69°C, 66-68°C or 66-67°C, 75-80°C (such as 76-79°C, 76-78°C or 76°C) Add 10% of the total molar amount of the second batch of polydiamines to the temperature gradient of -77°C), continue to stir and monitor the viscosity of the resin solution. If the viscosity of the resin is stable within the specified value range, stop feeding; otherwise, continue to add the remaining Two batches of the polydiamine were obtained until the resin viscosity reached the specified value.
为控制含氟封端剂的加入量,可进一步限定含氟封端剂摩尔总量加上第一批多元二胺、第二批多元二胺摩尔量约等于多元二酐摩尔量。In order to control the added amount of the fluorine-containing end-capping agent, the total molar amount of the fluorine-containing end-capping agent plus the first batch of polyvalent diamine and the second batch of polyvalent diamine can be further limited to be approximately equal to the molar amount of polyvalent dianhydride.
本公开在制备方法中,强调使用至少由两种二胺组成的多元二胺、至少由两种二酐组成的多元二酐,多元共聚的方式搭配不同的酐胺摩尔配比能够调节热膨胀系数,使得制备的聚酰亚胺树脂溶液在成膜后的热膨胀系数能够与基膜相当,以避免因膨胀系数相差较大薄膜边缘会出现卷缩现象。第一种二胺:……:第n种二胺=(0.1-0.9):……:(0.1-0.9),第一种二酐:……:第n种二酐=(0.1-0.9):……:(0.1-0.9),n≥2;就如表1所示,在相同多元二胺、多元二酐下,通过改变多元二胺之间的配比,以及多元二酐之间的配比,能够得到热膨胀系数不同的聚酰亚胺膜。In the preparation method of the present disclosure, it is emphasized to use a polyvalent diamine composed of at least two kinds of diamines, and a polybasic dianhydride composed of at least two kinds of dianhydrides, and the multi-component copolymerization mode with different molar ratios of anhydrides and amines can adjust the thermal expansion coefficient, The thermal expansion coefficient of the prepared polyimide resin solution after film formation can be equal to that of the base film, so as to avoid the phenomenon of curling at the edge of the film due to a large difference in the expansion coefficient. The first diamine: ...: the nth diamine = (0.1-0.9): ...: (0.1-0.9), the first dianhydride: ...: the nth dianhydride = (0.1-0.9) :...: (0.1-0.9), n≥2; as shown in Table 1, under the same polybasic diamine and polybasic dianhydride, by changing the ratio between polybasic diamines and the ratio between polybasic dianhydrides Mixing ratios can obtain polyimide films with different thermal expansion coefficients.
其中,本公开对二胺无特殊限制,可以为本领域任意公知的二胺,具体可以列举的有对苯二胺及其环上氟代化合物、联苯胺及其环上氟代化合物、4,4'-氧基二苯胺、1,3-双(4-氨基苯氧基)苯、1,3-双(3-氨基苯氧基)苯、1,3-双(2-氨基苯氧基)苯、4,4'-双(3-氨基苯氧基)联苯、4,4'-双(4-氨基苯氧基)联苯、4,4'-双(5-氨基苯氧基)联苯、双(4-(4-氨基苯氧基)苯基)砜、双(4-(3-氨基苯氧基)苯基)砜、双(4-(2-氨基苯氧基)苯基)砜、4,4'-二氨基二苯基乙烷、4,4'-二氨基二苯基异丙烷、4,4'-二氨基苯硫醚、3,3'-二氨基二苯砜、4,4'-二氨基二苯砜、3,3'-氧基二苯胺、3,4'-氧基二苯胺、2,4'-氧基二苯胺、4,4'-二氨基二苯基二乙基硅 烷、4,4'-二氨基二苯基硅烷、4,4'-二氨基二苯基乙基氧膦、4,4'-二氨基二苯基N-甲胺、4,4'-二氨基二苯基N-苯胺、1,3-二氨基苯、1,2-二氨基苯、2,2'-双[4-(4-氨基苯氧基)苯基]丙烷、2,2'-双[4-(4-氨基苯氧基)苯基]-1,1,1,3,3,3-六氟丙烷、4,4'-二氨基-2,2'-双三氟甲基联苯。Wherein, the present disclosure has no special restrictions on the diamine, which can be any well-known diamine in the art, specifically, p-phenylenediamine and its ring fluorinated compound, benzidine and its ring fluorinated compound, 4, 4'-Oxydiphenylamine, 1,3-bis(4-aminophenoxy)benzene, 1,3-bis(3-aminophenoxy)benzene, 1,3-bis(2-aminophenoxy) ) benzene, 4,4'-bis(3-aminophenoxy)biphenyl, 4,4'-bis(4-aminophenoxy)biphenyl, 4,4'-bis(5-aminophenoxy) ) biphenyl, bis(4-(4-aminophenoxy)phenyl)sulfone, bis(4-(3-aminophenoxy)phenyl)sulfone, bis(4-(2-aminophenoxy) phenyl) sulfone, 4,4'-diaminodiphenylethane, 4,4'-diaminodiphenylisopropane, 4,4'-diaminophenyl sulfide, 3,3'-diaminodiphenyl Phenylsulfone, 4,4'-diaminodiphenylsulfone, 3,3'-oxydiphenylamine, 3,4'-oxydiphenylamine, 2,4'-oxydiphenylamine, 4,4'-diphenylamine Aminodiphenyldiethylsilane, 4,4'-diaminodiphenylsilane, 4,4'-diaminodiphenylethylphosphine oxide, 4,4'-diaminodiphenyl N-methylamine , 4,4'-diaminodiphenyl N-aniline, 1,3-diaminobenzene, 1,2-diaminobenzene, 2,2'-bis[4-(4-aminophenoxy)phenyl ] propane, 2,2'-bis[4-(4-aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoropropane, 4,4'-diamino-2, 2'-bistrifluoromethylbiphenyl.
本公开对二酐无特殊限制,可以为本领域任意公知的二酐,具体可以列举的有均苯四羧酸二酐、2,3,6,7-四羧酸二酐、3,3',4,4'-联苯四羧酸二酐、1,2,5,6-萘四羧酸二酐、2,2',3,3'-联苯四羧酸二酐、2,2-双(3,4-二羧苯基)丙烷二酐、3,4,9,10-四羧酸二酐、双(3,4-二羧苯基)丙烷二酐、1,1-双(2,3-二羧苯基)乙烷二酐、1,1-双(3,4-二羧苯基)乙烷二酐、双(2,3-二羧苯基)甲烷二酐、双(3,4-二羧苯基)乙烷二酐、羟基二邻苯二甲酸二酐、双(3,4-二羧苯基)砜二酐、亚乙基双(偏苯三酸单酯酸酐)、双酚A双(偏苯三酸单酯酸酐)、4,4'-氧双邻苯二甲酸酐、4,4'-硫双邻苯二甲酸酐、3,3',4,4'-二苯酮四酸二酐、4,4'-氧双邻苯二甲酸酐、4,4'-(六氟异亚丙基)二邻苯二甲酸酐。There is no special limitation on the dianhydride in the present disclosure, and it can be any dianhydride known in the art, and specific examples include pyromellitic dianhydride, 2,3,6,7-tetracarboxylic dianhydride, 3,3' ,4,4'-biphenyltetracarboxylic dianhydride, 1,2,5,6-naphthalenetetracarboxylic dianhydride, 2,2',3,3'-biphenyltetracarboxylic dianhydride, 2,2 -Bis(3,4-dicarboxyphenyl)propane dianhydride, 3,4,9,10-tetracarboxylic dianhydride, bis(3,4-dicarboxyphenyl)propane dianhydride, 1,1-bis (2,3-Dicarboxyphenyl)ethanedianhydride, 1,1-bis(3,4-dicarboxyphenyl)ethanedianhydride, bis(2,3-dicarboxyphenyl)methane dianhydride, Bis(3,4-dicarboxyphenyl)ethane dianhydride, hydroxydiphthalic acid dianhydride, bis(3,4-dicarboxyphenyl)sulfone dianhydride, ethylenebis(trimellitic acid mono ester anhydride), bisphenol A bis (trimellitic acid monoester anhydride), 4,4'-oxybisphthalic anhydride, 4,4'-thiobisphthalic anhydride, 3,3',4 ,4'-benzophenone tetraacid dianhydride, 4,4'-oxydiphthalic anhydride, 4,4'-(hexafluoroisopropylidene)diphthalic anhydride.
本公开的含氟封端剂为含氟的单胺类芳香型有机物,与聚酰亚胺树脂溶液的端链酸酐结构反应进行端链封端,这样聚酰亚胺树脂溶液的端链结构就是含氟封端剂的氨基结构,从而避免聚酰亚胺树脂溶液水解,含氟封端剂可以列举的有间二(三氟甲基)苯胺、4-(4'-氟苯基)苯甲腈、对三氟甲基苯胺、2,6-二氟-3-甲基苯胺、氰基乙酰对三氟甲基苯胺、4-甲基-2-(三氟甲基)苯胺、3-氟-2-(三氟甲基)苯胺、5-氟-2-三氟甲基苯胺、4-氟-2-硝基-5-(三氟甲基)-苯胺、2,2'-二(三氟甲基)二氨基联苯、三氟苯胺、N-乙基-2,3,5-三氟苯胺、2,2'-二(3,4,5-三氟苯基)-4,4'-联苯二胺、2,3,4-三氟苯乙酰胺、2,3,4-三氟-6-硝基苯胺中的任意一种。The fluorine-containing end-capping agent of the present disclosure is a fluorine-containing monoamine aromatic organic compound, which reacts with the end-chain anhydride structure of the polyimide resin solution to perform end-chain end-capping, so that the end-chain structure of the polyimide resin solution is The amino structure of the fluorine-containing end-capping agent, so as to avoid the hydrolysis of the polyimide resin solution, the fluorine-containing end-capping agent can be listed as m-bis(trifluoromethyl)aniline, 4-(4'-fluorophenyl)benzyl Nitrile, p-trifluoromethylaniline, 2,6-difluoro-3-methylaniline, cyanoacetyl p-trifluoromethylaniline, 4-methyl-2-(trifluoromethyl)aniline, 3-fluoro -2-(trifluoromethyl)aniline, 5-fluoro-2-trifluoromethylaniline, 4-fluoro-2-nitro-5-(trifluoromethyl)-aniline, 2,2'-bis( Trifluoromethyl)diaminobiphenyl, trifluoroaniline, N-ethyl-2,3,5-trifluoroaniline, 2,2'-bis(3,4,5-trifluorophenyl)-4, Any of 4'-biphenylenediamine, 2,3,4-trifluorophenylacetamide, and 2,3,4-trifluoro-6-nitroaniline.
本公开对溶剂不做特殊限制,可以列举的有N,N-二甲基甲酰胺、N,N-二甲基乙酰胺、N-甲基吡咯烷酮、环己烷、甲基环己烷、四氢呋喃、异己烷、正庚烷、二氯甲烷、三氯乙烯、四氯化碳、环氧氯丙烷、甲基丙烯酸甲酯、二甲亚砜。The present disclosure does not make any special limitation on solvents, which can be listed as N,N-dimethylformamide, N,N-dimethylacetamide, N-methylpyrrolidone, cyclohexane, methylcyclohexane, tetrahydrofuran , isohexane, n-heptane, dichloromethane, trichloroethylene, carbon tetrachloride, epichlorohydrin, methyl methacrylate, dimethyl sulfoxide.
在得到粘度稳定强的聚酰亚胺树脂溶液后,更期望得到性能更加优异的薄膜,具体的制备方法为,采用上述任一技术方案得到的聚酰亚胺树脂溶液,在聚酰亚胺树脂溶液中依次加入催化剂、脱水剂让聚酰亚胺酸快速脱水亚胺化成膜,提高生产效率,涂覆在基膜的至少一侧时,增加薄膜拉伸强度。After obtaining a polyimide resin solution with strong viscosity stability, it is more desirable to obtain a film with better performance. A catalyst and a dehydrating agent are sequentially added to the solution to rapidly dehydrate and imidize the polyimide acid to form a film, so as to improve the production efficiency. When coated on at least one side of the base film, the tensile strength of the film is increased.
在本领域常用的催化剂类型基础上,本公开还扩充有本领域目前并未使 用到的催化剂类型,本公开强调催化剂可为单环或者稠环化合物,例如哒嗪、嘧啶、砒嗪、酞嗪亦、1,10-菲咯啉,如表1所示,在选用本公开强调的催化剂时,能够得到拉伸强度更为优异的聚酰亚胺膜,可选的,选用哒嗪和吡啶联合催化性能最优异,两种催化剂质量比1:4。On the basis of the catalyst types commonly used in the art, the present disclosure also expands the catalyst types that are not currently used in the art. The present disclosure emphasizes that the catalyst can be a monocyclic or condensed ring compound, such as pyridazine, pyrimidine, pyridine, phthalazine Also, 1,10-phenanthroline, as shown in Table 1, when the catalyst emphasized in this disclosure is selected, a polyimide film with more excellent tensile strength can be obtained. Optionally, a combination of pyridazine and pyridine can be selected. The catalytic performance is the best, and the mass ratio of the two catalysts is 1:4.
在制备过程中,可控制催化剂与聚酰亚胺树脂溶液的最佳配比是控制两者质量比在1:95-105范围内。In the preparation process, the optimal ratio of the controllable catalyst and the polyimide resin solution is to control the mass ratio of the two within the range of 1:95-105.
上述基膜不做特殊限制,可以为本领域常用的基膜,例如碳纳米纤维铜箔、碳纳米纤维银箔、碳纳米纤维铝箔、碳纳米纤维金箔,但由于碳纳米纤维铜箔散热性能优异,强度高,化学性质异常稳定,价格低廉等特点可以极好的解决线路板散热和氧化问题,并节约成本,由此在一些典型的实施方式中,基膜可以为碳纳米纤维铜箔。The above-mentioned base films are not particularly limited, and can be base films commonly used in the field, such as carbon nanofiber copper foil, carbon nanofiber silver foil, carbon nanofiber aluminum foil, carbon nanofiber gold foil, but due to the excellent heat dissipation performance of carbon nanofiber copper foil , high strength, extremely stable chemical properties, low price and other characteristics can solve the problem of heat dissipation and oxidation of circuit boards, and save costs, so in some typical embodiments, the base film can be carbon nanofiber copper foil.
本公开提供的制备方法可以使得聚酰亚胺在长期存储下性能、粘度均稳定。The preparation method provided by the present disclosure can make the polyimide stable in performance and viscosity under long-term storage.
本公开的制备方法解决粘度控制和粘度稳定的问题,本制备方法得到的聚酰亚胺树脂均一稳定,能够较长期在常温常压自然环境下保存而粘度和性能几乎不发生改变;含氟封端剂解决端链酸酐容易水解的问题,通过加入合适摩尔比例的单胺类芳香型有机物进行端链封端,端链结构为氨基结构,完全避免端基被水解的问题,同时解决普通聚酰亚胺树脂介电常数较高的问题,因为含氟化合物具有降低介电常数的作用,所以通过添加适量含氟胺类有机物可以有效降低介电常数,从而降低集成电路的漏电、发热以及导线间电容效应。The preparation method of the present disclosure solves the problems of viscosity control and viscosity stability. The polyimide resin obtained by the preparation method is uniform and stable, and can be stored in a natural environment at normal temperature and pressure for a long time without changing the viscosity and performance; The end agent solves the problem that the acid anhydride of the end chain is easy to be hydrolyzed. The end chain is capped by adding a suitable molar ratio of monoamine aromatic organic compounds. The end chain structure is an amino structure, which completely avoids the problem of the end group being hydrolyzed. The problem of high dielectric constant of imine resins is because fluorine-containing compounds have the effect of reducing the dielectric constant. Therefore, by adding an appropriate amount of fluorine-containing amine organic compounds, the dielectric constant can be effectively reduced, thereby reducing the leakage, heat generation of integrated circuits and between wires. capacitive effect.
使用本公开制备的聚酰亚胺树脂涂覆于基膜上制备薄膜时,形成的聚酰亚胺涂层热稳定性较强、热膨胀系数与基膜接近,解决因热膨胀系数相差较大而产生的薄膜边缘容易卷缩的问题。When the polyimide resin prepared by the present disclosure is coated on the base film to prepare a film, the formed polyimide coating has strong thermal stability, and the thermal expansion coefficient is close to that of the base film. The film edge is prone to curling.
实施例Example
实施例1Example 1
称量245.98g N,N-二甲基甲酰胺(分析纯)与高纯氮气氛围的烧瓶内,称取0.09981mol对苯二胺和0.04275mol 4,4'-二苯醚二胺与烧瓶内溶解完全;称取0.01500mol 3,3',4,4'-联苯四甲酸二酐和0.13509mol均苯四甲酸二酐混合加入烧瓶内,反应温度控制为0℃左右。Weigh 245.98g N,N-dimethylformamide (analytical grade) into a flask with high-purity nitrogen atmosphere, weigh 0.09981mol p-phenylenediamine and 0.04275mol 4,4'-diphenyl ether diamine into the flask Dissolve completely; weigh 0.01500mol 3,3',4,4'-biphenyltetracarboxylic dianhydride and 0.13509mol pyromellitic dianhydride and mix them into the flask, and control the reaction temperature to be about 0°C.
反应120min后,水浴开始升温到80℃,称取0.00528mol对苯二胺和 0.00225mol 4,4'-二苯醚二胺在氮气氛围下溶于20g N,N-二甲基甲酰胺,将所配置混合液采用差量法先多后少多次添加原则,30℃-35℃添加40%,45℃-50℃添加25%,65℃-70℃添加20%,75℃-80℃添加10%,剩余部分温度到80℃搅拌1h后视粘度状况而添加,搅拌速率15rad/min,控制PAA表观粘度在200000cP左右,充分反应240min后,加入1.38%摩尔比的间二(三氟甲基)苯胺封端,再充分反应60min后,降温至室温,称取86.02gN,N-二甲基甲酰胺将树脂粘度逐步稀释到50000cP左右,取100g稀释后的树脂,加入0.2g哒嗪和0.8g吡啶,匀速搅拌5min后,高真空快速脱泡,采用流延法分别在玻璃基板和碳纳米纤维铜箔上涂膜(薄膜厚度控制在20μm左右),化学亚胺化后在250℃无氧真空烘箱除去乙酸酐和溶剂。测试薄膜拉伸强度、热膨胀系数、吸水率、介电常数、边缘卷曲度。剩余树脂常温常压下密封保存,一个月后检测粘度。After the reaction for 120min, the water bath began to heat up to 80°C, and 0.00528mol of p-phenylenediamine and 0.00225mol of 4,4'-diphenyletherdiamine were weighed and dissolved in 20g of N,N-dimethylformamide under a nitrogen atmosphere. The prepared mixed solution adopts the principle of adding more first and then less multiple times, adding 40% at 30°C-35°C, adding 25% at 45°C-50°C, adding 20% at 65°C-70°C, and adding at 75°C-80°C 10%, the remaining part is added at a temperature of 80 °C and stirred for 1 hour, depending on the viscosity. The stirring rate is 15rad/min. base) aniline end-capped, fully reacted for 60min, cooled to room temperature, weighed 86.02g N,N-dimethylformamide to gradually dilute the resin viscosity to about 50000cP, took 100g of the diluted resin, added 0.2g pyridazine and 0.8g of pyridine, stirred at a constant speed for 5 minutes, and then quickly degassed in high vacuum. The glass substrate and the carbon nanofiber copper foil were coated by casting method (the thickness of the film was controlled at about 20μm). Oxygen vacuum oven removed acetic anhydride and solvent. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
实施例2Example 2
称量307.85g N,N-二甲基甲酰胺(分析纯)与高纯氮气氛围的烧瓶内,称取0.08321mol对苯二胺和0.08321mol 4,4'-二苯醚二胺与烧瓶内溶解完全;称取0.03502mol 3,3',4,4'-联苯四甲酸二酐和0.14007mol均苯四甲酸二酐混合加入烧瓶内,反应温度控制为0℃左右。反应120min后,水浴升温到80℃,称取0.00438mol对苯二胺和0.00438mol 4,4'-二苯醚二胺在氮气氛围下溶于4g N,N-二甲基甲酰胺,将所配置混合液采用差量法先多后少多次添加原则,30℃-35℃添加40%,45℃-50℃添加25%,65℃-70℃添加20%,75℃-80℃添加10%,剩余部分温度到80℃搅拌1h后视粘度状况而添加,搅拌速率15rad/min,控制PAA表观粘度在200000cP左右,充分反应240min后,加入1.26%摩尔比的封端剂间二(三氟甲基)苯胺,再充分反应60min后,降温至室温,称取107.57gN,N-二甲基甲酰胺将树脂粘度逐步稀释到50000cP,取100g稀释后的树脂,加入0.2g哒嗪和0.8g吡啶,匀速搅拌5min后,高真空快速脱泡,采用流延法分别在玻璃基板和碳纳米纤维铜箔上涂膜(薄膜厚度控制在20μm左右),化学亚胺化后在250℃无氧真空烘箱除去乙酸酐和溶剂。测试薄膜拉伸强度、热膨胀系数、吸水率、介电常数、边缘卷曲度。剩余树脂常温常压下密封保存,一个月后检测粘度。Weigh 307.85g N,N-dimethylformamide (analytical grade) into a flask with high-purity nitrogen atmosphere, and weigh 0.08321mol p-phenylenediamine and 0.08321mol 4,4'-diphenylether diamine into the flask Dissolved completely; weigh 0.03502mol 3,3',4,4'-biphenyltetracarboxylic dianhydride and 0.14007mol pyromellitic dianhydride and mix them into the flask, and control the reaction temperature to be about 0°C. After the reaction for 120min, the water bath was heated to 80°C, and 0.00438mol p-phenylenediamine and 0.00438mol 4,4'-diphenyletherdiamine were weighed and dissolved in 4g N,N-dimethylformamide under nitrogen atmosphere. To configure the mixed solution, the difference method is used to add more first and then less. Add 40% at 30°C-35°C, 25% at 45°C-50°C, 20% at 65°C-70°C, and 10% at 75°C-80°C. %, the remaining part is added at a temperature of 80 °C and stirred for 1 hour depending on the viscosity. The stirring rate is 15rad/min. Fluoromethyl)aniline, fully reacted for 60min, cooled to room temperature, weighed 107.57g N,N-dimethylformamide to gradually dilute the resin viscosity to 50000cP, took 100g of the diluted resin, added 0.2g pyridazine and 0.8g g pyridine, stir at a constant speed for 5 min, and then rapidly defoam in high vacuum. Coat the glass substrate and carbon nanofiber copper foil by casting method (the thickness of the film is controlled at about 20 μm). The acetic anhydride and solvent were removed in a vacuum oven. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
实施例3Example 3
称量291.95g N,N-二甲基甲酰胺(分析纯)与高纯氮气氛围的烧瓶内,称 取0.09509mol对苯二胺和0.06332mol 4,4'-二苯醚二胺与烧瓶内溶解完全;称取0.05003mol 3,3',4,4'-联苯四甲酸二酐和0.11674mol均苯四甲酸二酐混合加入烧瓶内,反应温度控制为0℃左右。反应120min后,水浴升温到80℃,称取0.00500mol对苯二胺和0.00333mol 4,4'-二苯醚二胺在氮气氛围下溶于4g N,N-二甲基甲酰胺,将所配置混合液采用差量法先多后少多次添加原则,30℃-35℃添加40%,45℃-50℃添加25%,65℃-70℃添加20%,75℃-80℃添加10%,剩余部分温度到80℃搅拌1h后视粘度状况而添加,搅拌速率15rad/min,控制PAA表观粘度在200000cP左右,充分反应240min后,加入0.79%摩尔比的封端剂间二(三氟甲基)苯胺,再充分反应60min,降温至室温,称取166.37gN,N-二甲基甲酰胺将树脂粘度逐步稀释到50000cP,取100g稀释后的树脂,加入0.2g哒嗪和0.8g吡啶,匀速搅拌5min后,高真空快速脱泡,采用流延法分别在玻璃基板和碳纳米纤维铜箔上涂膜(薄膜厚度控制在20μm左右),化学亚胺化后在250℃无氧真空烘箱除去乙酸酐和溶剂。测试薄膜拉伸强度、热膨胀系数、吸水率、介电常数、边缘卷曲度。剩余树脂常温常压下密封保存,一个月后检测粘度。Weigh 291.95g of N,N-dimethylformamide (analytical grade) in a flask with a high-purity nitrogen atmosphere, weigh 0.09509mol p-phenylenediamine and 0.06332mol 4,4'-diphenyl ether diamine into the flask Dissolved completely; weigh 0.05003mol 3,3',4,4'-biphenyltetracarboxylic dianhydride and 0.11674mol pyromellitic dianhydride and mix them into the flask, and control the reaction temperature to be about 0°C. After the reaction for 120min, the water bath was heated to 80°C, and 0.00500mol p-phenylenediamine and 0.00333mol 4,4'-diphenyletherdiamine were weighed and dissolved in 4g N,N-dimethylformamide under nitrogen atmosphere. To configure the mixed solution, the difference method is used to add more first and then less. Add 40% at 30°C-35°C, 25% at 45°C-50°C, 20% at 65°C-70°C, and 10% at 75°C-80°C. %, the remaining part is added at a temperature of 80 °C and stirred for 1 hour depending on the viscosity. The stirring rate is 15rad/min. Fluoromethyl)aniline, fully reacted for 60min, cooled to room temperature, weighed 166.37g N,N-dimethylformamide to gradually dilute the resin viscosity to 50000cP, took 100g of the diluted resin, added 0.2g pyridazine and 0.8g Pyridine, stirred at a constant speed for 5 minutes, then rapidly degassed in high vacuum, and coated on glass substrate and carbon nanofiber copper foil by casting method (film thickness was controlled at about 20 μm), and after chemical imidization, oxygen-free vacuum at 250 °C was used. The oven removes acetic anhydride and solvent. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
实施例4Example 4
称量305.89g N,N-二甲基甲酰胺(分析纯)与高纯氮气氛围的烧瓶内,称取0.06342mol对苯二胺和0.09500mol 4,4'-二苯醚二胺与烧瓶内溶解完全;称取0.05003mol 3,3',4,4'-联苯四甲酸二酐和0.11674mol均苯四甲酸二酐混合加入烧瓶内,反应温度控制为0℃左右。反应120min后,水浴升温到80℃,称取0.00334mol对苯二胺和0.00500mol 4,4'-二苯醚二胺在氮气氛围下溶于4g N,N-二甲基甲酰胺,将所配置混合液采用差量法先多后少多次添加原则,30℃-35℃添加40%,45℃-50℃添加25%,65℃-70℃添加20%,75℃-80℃添加10%,剩余部分温度到80℃搅拌1h后视粘度状况而添加,搅拌速率15rad/min,控制PAA表观粘度在200000cP左右,充分反应240min后,加入1.34%摩尔比的封端剂间二(三氟甲基)苯胺,再充分反应60min,降温至室温,称取106.95gN,N-二甲基甲酰胺将树脂粘度逐步稀释到50000cP,取100g稀释后的树脂,加入0.2g哒嗪和0.8g吡啶,匀速搅拌5min后,高真空快速脱泡,采用流延法分别在玻璃基板和碳纳米纤维铜箔上涂膜(薄膜厚度控制在20μm左右),化学亚胺化后在250℃无氧真空烘箱除去乙酸酐和溶剂。测试薄膜拉伸强度、热膨胀系数、吸水率、介电常数、边缘卷曲度。剩余树脂 常温常压下密封保存,一个月后检测粘度。Weigh 305.89g of N,N-dimethylformamide (analytical grade) in a flask with high-purity nitrogen atmosphere, weigh 0.06342mol p-phenylenediamine and 0.09500mol 4,4'-diphenyletherdiamine into the flask Dissolved completely; weigh 0.05003mol 3,3',4,4'-biphenyltetracarboxylic dianhydride and 0.11674mol pyromellitic dianhydride and mix them into the flask, and control the reaction temperature to be about 0°C. After the reaction for 120min, the water bath was heated to 80°C, and 0.00334mol p-phenylenediamine and 0.00500mol 4,4'-diphenyletherdiamine were weighed and dissolved in 4g N,N-dimethylformamide under nitrogen atmosphere. To configure the mixed solution, the difference method is used to add more first and then less. Add 40% at 30°C-35°C, 25% at 45°C-50°C, 20% at 65°C-70°C, and 10% at 75°C-80°C. %, the remaining part is added at a temperature of 80 °C and stirred for 1 hour depending on the viscosity. The stirring rate is 15 rad/min. Fluoromethyl)aniline, fully reacted for 60min, cooled to room temperature, weighed 106.95g N,N-dimethylformamide to gradually dilute the resin viscosity to 50000cP, took 100g of the diluted resin, added 0.2g pyridazine and 0.8g Pyridine, stirred at a constant speed for 5 minutes, then rapidly degassed in high vacuum, and coated on glass substrate and carbon nanofiber copper foil by casting method (film thickness was controlled at about 20 μm), and after chemical imidization, oxygen-free vacuum at 250 °C was used. The oven removes acetic anhydride and solvent. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is checked after one month.
实施例5Example 5
称量223.04g N,N-二甲基甲酰胺(分析纯)与高纯氮气氛围的烧瓶内,称取0.07134mol对苯二胺和0.04750mol 4,4'-二苯醚二胺与烧瓶内溶解完全;称取0.05003mol 3,3',4,4'-联苯四甲酸二酐和0.07505mol均苯四甲酸二酐混合加入烧瓶内,反应温度控制为0℃左右。反应120min后,水浴升温到80℃,称取0.00375mol对苯二胺和0.00250mol 4,4'-二苯醚二胺在氮气氛围下溶于4g N,N-二甲基甲酰胺,将所配置混合液采用差量法先多后少多次添加原则,30℃-35℃添加40%,45℃-50℃添加25%,65℃-70℃添加20%,75℃-80℃添加10%,剩余部分温度到80℃搅拌1h后视粘度状况而添加,搅拌速率15rad/min,控制PAA表观粘度在200000cP左右,充分反应240min后,加入0.98%摩尔比的封端剂间二(三氟甲基)苯胺,再充分反应60min,降温至室温,称取127.25gN,N-二甲基甲酰胺将树脂粘度逐步稀释到50000cP,取100g稀释后的树脂,加入0.2g哒嗪和0.8g吡啶,匀速搅拌5min后,高真空快速脱泡,采用流延法分别在玻璃基板和碳纳米纤维铜箔上涂膜(薄膜厚度控制在20μm左右),化学亚胺化后在250℃无氧真空烘箱除去乙酸酐和溶剂。测试薄膜拉伸强度、热膨胀系数、吸水率、介电常数、边缘卷曲度。剩余树脂常温常压下密封保存,一个月后检测粘度。Weigh 223.04g of N,N-dimethylformamide (analytical grade) in a flask with a high-purity nitrogen atmosphere, weigh 0.07134mol p-phenylenediamine and 0.04750mol 4,4'-diphenylether diamine into the flask Dissolve completely; weigh 0.05003mol 3,3',4,4'-biphenyltetracarboxylic dianhydride and 0.07505mol pyromellitic dianhydride and mix them into the flask, and control the reaction temperature to be about 0°C. After the reaction for 120min, the water bath was heated to 80°C, and 0.00375mol p-phenylenediamine and 0.00250mol 4,4'-diphenyletherdiamine were weighed and dissolved in 4g N,N-dimethylformamide under nitrogen atmosphere. To configure the mixed solution, the difference method is used to add more first and then less. Add 40% at 30°C-35°C, 25% at 45°C-50°C, 20% at 65°C-70°C, and 10% at 75°C-80°C. %, the remaining part is added at a temperature of 80 °C and stirred for 1 hour, depending on the viscosity. The stirring rate is 15rad/min. Fluoromethyl)aniline, fully reacted for 60min, cooled to room temperature, weighed 127.25g N,N-dimethylformamide to gradually dilute the resin viscosity to 50000cP, took 100g of the diluted resin, added 0.2g pyridazine and 0.8g Pyridine, stirred at a constant speed for 5 minutes, then rapidly degassed in high vacuum, and coated on glass substrate and carbon nanofiber copper foil by casting method (film thickness was controlled at about 20 μm), and after chemical imidization, oxygen-free vacuum at 250 °C was used. The oven removes acetic anhydride and solvent. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
对比例1Comparative Example 1
称量245.98g N,N-二甲基甲酰胺(分析纯)与高纯氮气氛围的烧瓶内,称取0.09981mol对苯二胺和0.04275mol 4,4'-二苯醚二胺与烧瓶内溶解完全;称取0.01500mol 3,3',4,4'-联苯四甲酸二酐和0.13509mol均苯四甲酸二酐混合加入烧瓶内,反应温度控制为0℃左右。反应120min后,称取0.00528mol对苯二胺和0.00225mol 4,4'-二苯醚二胺在氮气氛围下溶于20g N,N-二甲基甲酰胺,将所配置混合液加入烧瓶,根据经验控制添加量,控制粘度200000cP左右,反应240min后,称取86.02gN,N-二甲基甲酰胺将树脂粘度逐步稀释到50000cP左右,取100g稀释后的树脂高真空快速脱泡,流延法玻璃基板上涂膜(薄膜厚度控制在20μm左右),在500℃无氧真空烘箱亚胺化成膜。测试薄膜拉伸强度、热膨胀系数、吸水率、介电常数、边缘卷曲度。剩余树脂常温常压下密封保存,一个月后检测粘度。Weigh 245.98g N,N-dimethylformamide (analytical grade) into a flask with high-purity nitrogen atmosphere, weigh 0.09981mol p-phenylenediamine and 0.04275mol 4,4'-diphenyl ether diamine into the flask Dissolve completely; weigh 0.01500mol 3,3',4,4'-biphenyltetracarboxylic dianhydride and 0.13509mol pyromellitic dianhydride and mix them into the flask, and control the reaction temperature to be about 0°C. After 120min of reaction, weigh 0.00528mol p-phenylenediamine and 0.00225mol 4,4'-diphenyl ether diamine and dissolve in 20g N,N-dimethylformamide under nitrogen atmosphere, add the configured mixed solution to the flask, Control the amount of addition according to experience, and control the viscosity to about 200,000cP. After 240min of reaction, weigh 86.02g of N,N-dimethylformamide to gradually dilute the resin viscosity to about 50,000cP. Take 100g of the diluted resin for rapid degassing in high vacuum and cast it. The film is coated on the glass substrate (the thickness of the film is controlled at about 20 μm), and the film is formed by imidization in an oxygen-free vacuum oven at 500 °C. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
对比例2Comparative Example 2
称量307.85g N,N-二甲基甲酰胺(分析纯)与高纯氮气氛围的烧瓶内,称取0.08321mol对苯二胺和0.08321mol 4,4'-二苯醚二胺与烧瓶内溶解完全;称取0.03502mol 3,3',4,4'-联苯四甲酸二酐和0.14007mol均苯四甲酸二酐混合加入烧瓶内,反应温度控制为0℃左右。反应120min后,称取0.00438mol对苯二胺和0.00438mol 4,4'-二苯醚二胺在氮气氛围下溶于4g N,N-二甲基甲酰胺,将所配置混合液加入烧瓶,根据经验控制添加量,控制粘度200000cP左右,反应240min后,称取86.02gN,N-二甲基甲酰胺将树脂粘度逐步稀释到50000cP左右,取100g稀释后的树脂高真空快速脱泡,流延法玻璃基板上涂膜(薄膜厚度控制在20μm左右),在500℃无氧真空烘箱亚胺化成膜。测试薄膜拉伸强度、热膨胀系数、吸水率、介电常数、边缘卷曲度。剩余树脂常温常压下密封保存,一个月后检测粘度。Weigh 307.85g N,N-dimethylformamide (analytical grade) into a flask with high-purity nitrogen atmosphere, and weigh 0.08321mol p-phenylenediamine and 0.08321mol 4,4'-diphenylether diamine into the flask Dissolved completely; weigh 0.03502mol 3,3',4,4'-biphenyltetracarboxylic dianhydride and 0.14007mol pyromellitic dianhydride and mix them into the flask, and control the reaction temperature to be about 0°C. After the reaction for 120min, 0.00438mol p-phenylenediamine and 0.00438mol 4,4'-diphenyl ether diamine were weighed and dissolved in 4g N,N-dimethylformamide under nitrogen atmosphere, and the configured mixed solution was added to the flask, Control the amount of addition according to experience, and control the viscosity to about 200,000cP. After 240min of reaction, weigh 86.02g of N,N-dimethylformamide to gradually dilute the resin viscosity to about 50,000cP. Take 100g of the diluted resin for rapid degassing in high vacuum and cast it. The film is coated on the glass substrate (the thickness of the film is controlled at about 20 μm), and the film is formed by imidization in an oxygen-free vacuum oven at 500 °C. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
对比例3Comparative Example 3
称量291.95g N,N-二甲基甲酰胺(分析纯)与高纯氮气氛围的烧瓶内,称取0.09509mol对苯二胺和0.06332mol 4,4'-二苯醚二胺与烧瓶内溶解完全;称取0.05003mol 3,3',4,4'-联苯四甲酸二酐和0.11674mol均苯四甲酸二酐混合加入烧瓶内,反应温度控制为0℃左右。反应120min后,称取0.00500mol对苯二胺和0.00333mol 4,4'-二苯醚二胺在氮气氛围下溶于4g N,N-二甲基甲酰胺,将所配置混合液加入烧瓶,根据经验控制添加量,控制粘度200000cP左右,反应240min后,称取86.02gN,N-二甲基甲酰胺将树脂粘度逐步稀释到50000cP左右,取100g稀释后的树脂高真空快速脱泡,流延法玻璃基板上涂膜(薄膜厚度控制在20μm左右),在500℃无氧真空烘箱亚胺化成膜。测试薄膜拉伸强度、热膨胀系数、吸水率、介电常数、边缘卷曲度。剩余树脂常温常压下密封保存,一个月后检测粘度。Weigh 291.95g of N,N-dimethylformamide (analytical grade) in a flask with a high-purity nitrogen atmosphere, weigh 0.09509mol p-phenylenediamine and 0.06332mol 4,4'-diphenyl ether diamine into the flask Dissolved completely; weigh 0.05003mol 3,3',4,4'-biphenyltetracarboxylic dianhydride and 0.11674mol pyromellitic dianhydride and mix them into the flask, and control the reaction temperature to be about 0°C. After 120min of reaction, weigh 0.00500mol p-phenylenediamine and 0.00333mol 4,4'-diphenyl ether diamine and dissolve in 4g N,N-dimethylformamide under nitrogen atmosphere, add the configured mixed solution to the flask, Control the amount of addition according to experience, and control the viscosity to about 200,000cP. After 240min of reaction, weigh 86.02g of N,N-dimethylformamide to gradually dilute the resin viscosity to about 50,000cP. Take 100g of the diluted resin for rapid degassing in high vacuum and cast it. The film is coated on the glass substrate (the thickness of the film is controlled at about 20 μm), and the film is formed by imidization in an oxygen-free vacuum oven at 500 °C. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
对比例4Comparative Example 4
称量305.89g N,N-二甲基甲酰胺(分析纯)与高纯氮气氛围的烧瓶内,称取0.06342mol对苯二胺和0.09500mol 4,4'-二苯醚二胺与烧瓶内溶解完全;称取0.05003mol 3,3',4,4'-联苯四甲酸二酐和0.11674mol均苯四甲酸二酐混合加入烧瓶内,反应温度控制为0℃左右。反应120min后,称取0.00334mol对苯二胺和0.00500mol 4,4'-二苯醚二胺在氮气氛围下溶于4g N,N-二甲基甲酰胺,将所配置混合液加入烧瓶,根据经验控制添加量,控制粘度200000cP左右,反应240min后,称取86.02gN,N-二甲基甲酰胺将树脂粘度逐步稀释到50000cP 左右,取100g稀释后的树脂高真空快速脱泡,流延法玻璃基板上涂膜(薄膜厚度控制在20μm左右),在500℃无氧真空烘箱亚胺化成膜。测试薄膜拉伸强度、热膨胀系数、吸水率、介电常数、边缘卷曲度。剩余树脂常温常压下密封保存,一个月后检测粘度。Weigh 305.89g of N,N-dimethylformamide (analytical grade) in a flask with high-purity nitrogen atmosphere, weigh 0.06342mol p-phenylenediamine and 0.09500mol 4,4'-diphenyletherdiamine into the flask Dissolved completely; weigh 0.05003mol 3,3',4,4'-biphenyltetracarboxylic dianhydride and 0.11674mol pyromellitic dianhydride and mix them into the flask, and control the reaction temperature to be about 0°C. After the reaction for 120min, 0.00334mol p-phenylenediamine and 0.00500mol 4,4'-diphenyl ether diamine were weighed and dissolved in 4g N,N-dimethylformamide under nitrogen atmosphere, and the configured mixed solution was added to the flask, Control the amount of addition according to experience, and control the viscosity to be about 200000cP. After 240min of reaction, weigh 86.02g N,N-dimethylformamide to gradually dilute the resin viscosity to about 50000cP, take 100g of the diluted resin and quickly defoam under high vacuum and cast it. The film is coated on the glass substrate (the thickness of the film is controlled at about 20 μm), and the film is formed by imidization in an oxygen-free vacuum oven at 500 °C. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
对比例5Comparative Example 5
称量223.04g N,N-二甲基甲酰胺(分析纯)与高纯氮气氛围的烧瓶内,称取0.07134mol对苯二胺和0.04750mol 4,4'-二苯醚二胺与烧瓶内溶解完全;称取0.05003mol 3,3',4,4'-联苯四甲酸二酐和0.07505mol均苯四甲酸二酐混合加入烧瓶内,反应温度控制为0℃左右。反应120min后,称取0.00375mol对苯二胺和0.00250mol 4,4'-二苯醚二胺在氮气氛围下溶于4g N,N-二甲基甲酰胺,将所配置混合液加入烧瓶,根据经验控制添加量,控制粘度200000cP左右,反应240min后,称取86.02gN,N-二甲基甲酰胺将树脂粘度逐步稀释到50000cP左右,取100g稀释后的树脂高真空快速脱泡,流延法玻璃基板上涂膜(薄膜厚度控制在20μm左右),在500℃无氧真空烘箱亚胺化成膜。测试薄膜拉伸强度、热膨胀系数、吸水率、介电常数、边缘卷曲度。剩余树脂常温常压下密封保存,一个月后检测粘度。Weigh 223.04g of N,N-dimethylformamide (analytical grade) in a flask with a high-purity nitrogen atmosphere, weigh 0.07134mol p-phenylenediamine and 0.04750mol 4,4'-diphenylether diamine into the flask Dissolve completely; weigh 0.05003mol 3,3',4,4'-biphenyltetracarboxylic dianhydride and 0.07505mol pyromellitic dianhydride and mix them into the flask, and control the reaction temperature to be about 0°C. After 120min of reaction, weigh 0.00375mol p-phenylenediamine and 0.00250mol 4,4'-diphenyl ether diamine and dissolve in 4g N,N-dimethylformamide under nitrogen atmosphere, add the configured mixed solution to the flask, Control the amount of addition according to experience, and control the viscosity to about 200,000cP. After 240min of reaction, weigh 86.02g of N,N-dimethylformamide to gradually dilute the resin viscosity to about 50,000cP. Take 100g of the diluted resin for rapid degassing in high vacuum and cast it. The film is coated on the glass substrate (the thickness of the film is controlled at about 20 μm), and the film is formed by imidization in an oxygen-free vacuum oven at 500 °C. Test the film tensile strength, thermal expansion coefficient, water absorption, dielectric constant, edge curl. The remaining resin is sealed and stored under normal temperature and pressure, and the viscosity is tested after one month.
表1Table 1
Figure PCTCN2022089436-appb-000001
Figure PCTCN2022089436-appb-000001
Figure PCTCN2022089436-appb-000002
Figure PCTCN2022089436-appb-000002
Figure PCTCN2022089436-appb-000003
Figure PCTCN2022089436-appb-000003
Figure PCTCN2022089436-appb-000004
Figure PCTCN2022089436-appb-000004
由上表可知,对比例1-5在不添加封端剂也不做其他控制条件的情况下,初始表观粘度控制比较困难,粘度跨度较大,极不稳定,重复性较差。常温保存一个月后树脂粘度下降十分明显,而本公开实施例1-5制备的聚酰亚胺树脂溶液当二胺添加比例控制在98.6%~99.3%,封端剂添加比例控制在1.4%~0.7%,初始表观粘度可控制在300000cP左右,常温保存一个月后树脂粘度未发生较明显变化,粘度稳定性优异。It can be seen from the above table that the control of the initial apparent viscosity of Comparative Examples 1-5 is difficult without adding end-capping agent or other control conditions, the viscosity span is large, extremely unstable, and the repeatability is poor. After being stored at room temperature for one month, the viscosity of the resin decreases significantly, while the polyimide resin solution prepared in Examples 1-5 of the present disclosure is controlled at a diamine addition ratio of 98.6% to 99.3% and an end capping agent addition ratio of 1.4% to 1.4%. 0.7%, the initial apparent viscosity can be controlled at about 300,000cP, the viscosity of the resin does not change significantly after being stored at room temperature for one month, and the viscosity stability is excellent.
同时,对比例1-5所制得的薄膜拉伸强度较低,热膨胀系数与铜箔相差较大,吸水率高,介电常数较大,薄膜产生很明显卷曲现象,无法满足工业生产要求。而实施例1-5制备的聚酰亚胺树脂溶液单独制膜时,拉伸强度均大于120MPa,热膨胀系数接近铜箔(18×10-6k-1),吸水率较低,均小于2%,介电常数小于3,薄膜不产生卷曲现象,表明各项性能良好,在以石墨烯铜箔做为基膜时,所制备的薄膜拉伸强度极大增加超过320MPa,热膨胀系数接近铜箔(18×10-6k-1),吸水率较低,均小于2%,介电常数小于3,薄膜外侧产生极小卷曲现象,表明各项性能良好,满足微电子产品需要。At the same time, the films prepared in Comparative Examples 1-5 have low tensile strength, large difference in thermal expansion coefficient and copper foil, high water absorption, high dielectric constant, and obvious curling phenomenon of the film, which cannot meet the requirements of industrial production. However, when the polyimide resin solution prepared in Examples 1-5 was used to form a film alone, the tensile strength was greater than 120MPa, the thermal expansion coefficient was close to that of copper foil (18×10-6k-1), and the water absorption rate was low, all less than 2% , the dielectric constant is less than 3, the film does not produce curling phenomenon, indicating that the performance is good, when the graphene copper foil is used as the base film, the tensile strength of the prepared film is greatly increased by more than 320MPa, and the thermal expansion coefficient is close to that of copper foil ( 18×10-6k-1), the water absorption rate is low, less than 2%, the dielectric constant is less than 3, and the outer side of the film has a very small curling phenomenon, indicating that the performance is good and meets the needs of microelectronic products.
以上所述仅是本公开的可选的实施方式,应当指出,对于本技术领域的普通技术人员,在不脱离本公开构思的前提下,还可以做出若干改进和润饰 ,这些改进和润饰也应视为本公开的保护范围。The above are only optional embodiments of the present disclosure. It should be pointed out that for those skilled in the art, without departing from the concept of the present disclosure, several improvements and modifications can be made. It should be regarded as the protection scope of the present disclosure.
工业实用性Industrial Applicability
本公开提供了一种聚酰亚胺树脂的制备方法及其薄膜,本公开制备的聚酰亚胺具备长期存储下性能、粘度稳定的特性,同时本公开制备的聚酰亚胺树脂涂覆于基膜上制备薄膜时,形成的聚酰亚胺涂层热稳定性较强、热膨胀系数与基膜接近,解决因热膨胀系数相差较大而产生的薄膜边缘容易卷缩的问题。因此本公开制备的聚酰亚胺以及由此制备的薄膜具有优异的工业实用性能和良好的市场前景。The present disclosure provides a method for preparing polyimide resin and a film thereof. The polyimide prepared in the present disclosure has the characteristics of long-term storage performance and stable viscosity, and the polyimide resin prepared in the present disclosure is coated on When the film is prepared on the base film, the formed polyimide coating has strong thermal stability, and the thermal expansion coefficient is close to the base film, which solves the problem that the edge of the film is easily curled due to the large difference in the thermal expansion coefficient. Therefore, the polyimide prepared by the present disclosure and the film prepared therefrom have excellent industrial practical properties and good market prospects.

Claims (15)

  1. 一种聚酰亚胺树脂的制备方法,其特征在于,包括以下步骤:A preparation method of polyimide resin, comprising the following steps:
    S1、将第一批多元二胺在惰性气体氛围下溶解于溶剂中后,在30℃及以下的低温环境中加入105-110%第一批多元二胺摩尔总量的多元二酐先行聚合形成树脂溶液,控制树脂溶液粘度在50000-70000cps;S1. After dissolving the first batch of polyvalent diamines in a solvent under an inert gas atmosphere, add 105-110% of the first batch of polyvalent diamines in a low-temperature environment of 30 ° C and below, and then polymerize to form Resin solution, control the viscosity of resin solution at 50000-70000cps;
    S2、监控树脂溶液粘度并在30-80℃内逐步升温,将第二批多元二胺分批量先多后少逐步加入,直至树脂溶液粘度为180000-200000cps;S2. Monitor the viscosity of the resin solution and gradually increase the temperature within 30-80°C, and gradually add the second batch of polybasic diamines in batches, until the viscosity of the resin solution is 180000-200000cps;
    S3、加入含氟封端剂混合,高真空消泡后得到聚酰亚胺树脂溶液。S3, adding a fluorine-containing end-capping agent and mixing, and obtaining a polyimide resin solution after high-vacuum defoaming.
  2. 如权利要求1所述的聚酰亚胺树脂的制备方法,其特征在于,S1步骤中的低温环境为-20-30℃。The method for preparing polyimide resin according to claim 1, wherein the low temperature environment in step S1 is -20-30°C.
  3. 如权利要求1或2所述的聚酰亚胺树脂的制备方法,其特征在于,S2步骤中所述第二批多元二胺加入量为第一批多元二胺摩尔总量的5-10%,分批量加入具体操作为:30-35℃温度梯度内添加第二批多元二胺摩尔总量的40%,45-50℃温度梯度内添加第二批多元二胺摩尔总量的25%,65-70℃温度梯度内添加第二批多元二胺摩尔总量的20%,75-80℃温度梯度内添加第二批多元二胺摩尔总量的10%,持续搅拌并监测树脂溶液粘度,若树脂粘度稳定在180000-200000cps,则停止加料,反之,则继续添加剩余第二批多元二胺直至树脂粘度稳定在50000-70000cps。The preparation method of polyimide resin according to claim 1 or 2, wherein the second batch of polyvalent diamines added in step S2 is 5-10% of the first batch of polyvalent diamines in total moles , the specific operation of adding in batches is as follows: adding 40% of the total molar amount of the second batch of polyvalent diamines in a temperature gradient of 30-35 °C, adding 25% of the total molar amount of the second batch of polyvalent diamines in a temperature gradient of 45-50 °C, Add 20% of the total molar amount of the second batch of polyvalent diamines in a temperature gradient of 65-70 °C, add 10% of the total molar amount of the second batch of polyvalent diamines in a temperature gradient of 75-80 °C, continue stirring and monitor the viscosity of the resin solution, If the resin viscosity is stable at 180000-200000cps, stop feeding, otherwise, continue to add the remaining second batch of polydiamine until the resin viscosity is stable at 50000-70000cps.
  4. 如权利要求1-3中任一项所述的聚酰亚胺树脂的制备方法,其特征在于,含氟封端剂摩尔总量加上第一批多元二胺、第二批多元二胺摩尔量约等于多元二酐摩尔量。The preparation method of polyimide resin according to any one of claims 1-3, characterized in that, the molar amount of the fluorine-containing end capping agent is added to the moles of the first batch of polyvalent diamines and the second batch of polyvalent diamines. The amount is approximately equal to the molar amount of the polybasic dianhydride.
  5. 如权利要求1-4中任一项所述的聚酰亚胺树脂的制备方法,其特征在于,所述多元二胺包括对苯二胺及其环上氟代化合物、联苯胺及其环上氟代化合物、4,4'-氧基二苯胺、1,3-双(4-氨基苯氧基)苯、1,3-双(3-氨基苯氧基)苯、1,3-双(2-氨基苯氧基)苯、4,4'-双(3-氨基苯氧基)联苯、4,4'-双(4-氨基苯氧基)联苯、4,4'-双(5-氨基苯氧基)联苯、双(4-(4-氨基苯氧基)苯基)砜、双(4-(3-氨基苯氧基)苯基)砜、双(4-(2-氨基苯氧基)苯基)砜、4,4'-二氨基二苯基乙烷、4,4'-二氨基二苯基异丙烷、4,4'-二氨基苯硫醚、3,3'-二氨基二苯砜、4,4'-二氨基二苯砜、3,3'-氧基二苯胺、3,4'-氧基二苯胺、2,4'-氧基二苯胺、4,4'-二氨基二苯基二乙基硅烷、4,4'-二氨基二苯基硅烷、4,4'-二氨基二苯基乙基氧膦、4,4'-二 氨基二苯基N-甲胺、4,4'-二氨基二苯基N-苯胺、1,3-二氨基苯、1,2-二氨基苯、2,2'-双[4-(4-氨基苯氧基)苯基]丙烷、2,2'-双[4-(4-氨基苯氧基)苯基]-1,1,1,3,3,3-六氟丙烷、4,4'-二氨基-2,2'-双三氟甲基联苯的任意两种或多种配比。The method for preparing polyimide resin according to any one of claims 1-4, wherein the polyvalent diamine comprises p-phenylenediamine and its ring fluorinated compound, benzidine and its ring Fluorinated compounds, 4,4'-oxydiphenylamine, 1,3-bis(4-aminophenoxy)benzene, 1,3-bis(3-aminophenoxy)benzene, 1,3-bis(4-aminophenoxy)benzene 2-Aminophenoxy)benzene, 4,4'-bis(3-aminophenoxy)biphenyl, 4,4'-bis(4-aminophenoxy)biphenyl, 4,4'-bis( 5-Aminophenoxy)biphenyl, bis(4-(4-aminophenoxy)phenyl)sulfone, bis(4-(3-aminophenoxy)phenyl)sulfone, bis(4-(2) -Aminophenoxy)phenyl)sulfone, 4,4'-diaminodiphenylethane, 4,4'-diaminodiphenylisopropane, 4,4'-diaminophenyl sulfide, 3, 3'-diaminodiphenylsulfone, 4,4'-diaminodiphenylsulfone, 3,3'-oxydiphenylamine, 3,4'-oxydiphenylamine, 2,4'-oxydiphenylamine, 4,4'-diaminodiphenyldiethylsilane, 4,4'-diaminodiphenylsilane, 4,4'-diaminodiphenylethylphosphine oxide, 4,4'-diaminodiphenyl Phenyl N-methylamine, 4,4'-diaminodiphenyl N-aniline, 1,3-diaminobenzene, 1,2-diaminobenzene, 2,2'-bis[4-(4-amino Phenoxy)phenyl]propane, 2,2'-bis[4-(4-aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoropropane, 4,4' -Any two or more ratios of diamino-2,2'-bistrifluoromethylbiphenyl.
  6. 如权利要求1-5中任一项所述的聚酰亚胺树脂的制备方法,其特征在于,所述多元二酐包括均苯四羧酸二酐、2,3,6,7-四羧酸二酐、3,3',4,4'-联苯四羧酸二酐、1,2,5,6-萘四羧酸二酐、2,2',3,3'-联苯四羧酸二酐、2,2-双(3,4-二羧苯基)丙烷二酐、3,4,9,10-四羧酸二酐、双(3,4-二羧苯基)丙烷二酐、1,1-双(2,3-二羧苯基)乙烷二酐、1,1-双(3,4-二羧苯基)乙烷二酐、双(2,3-二羧苯基)甲烷二酐、双(3,4-二羧苯基)乙烷二酐、羟基二邻苯二甲酸二酐、双(3,4-二羧苯基)砜二酐、亚乙基双(偏苯三酸单酯酸酐)、双酚A双(偏苯三酸单酯酸酐)、4,4'-氧双邻苯二甲酸酐、4,4'-硫双邻苯二甲酸酐、3,3',4,4'-二苯酮四酸二酐、4,4'-氧双邻苯二甲酸酐、4,4'-(六氟异亚丙基)二邻苯二甲酸酐中的任意两种或多种配比。The preparation method of polyimide resin according to any one of claims 1-5, wherein the polyvalent dianhydride comprises pyromellitic dianhydride, 2,3,6,7-tetracarboxylic acid Acid dianhydride, 3,3',4,4'-biphenyltetracarboxylic dianhydride, 1,2,5,6-naphthalene tetracarboxylic dianhydride, 2,2',3,3'-biphenyltetracarboxylic acid Carboxylic dianhydride, 2,2-bis(3,4-dicarboxyphenyl)propane dianhydride, 3,4,9,10-tetracarboxylic dianhydride, bis(3,4-dicarboxyphenyl)propane Dianhydride, 1,1-bis(2,3-dicarboxyphenyl)ethanedianhydride, 1,1-bis(3,4-dicarboxyphenyl)ethanedianhydride, bis(2,3-dicarboxyphenyl)ethanedianhydride Carboxyphenyl)methane dianhydride, bis(3,4-dicarboxyphenyl)ethane dianhydride, hydroxydiphthalic dianhydride, bis(3,4-dicarboxyphenyl)sulfone dianhydride, ethylene bis(trimellitic acid monoester anhydride), bisphenol A bis(trimellitic acid monoester anhydride), 4,4'-oxybisphthalic anhydride, 4,4'-sulfur diphthalic anhydride Acid anhydride, 3,3',4,4'-benzophenone tetraacid dianhydride, 4,4'-oxydiphthalic anhydride, 4,4'-(hexafluoroisopropylidene)diphthalic acid Any two or more ratios in formic anhydride.
  7. 如权利要求1-6中任一项所述的聚酰亚胺树脂的制备方法,其特征在于所述含氟封端剂包括含氟的单胺类芳香型有机物。The method for preparing a polyimide resin according to any one of claims 1 to 6, wherein the fluorine-containing end-capping agent comprises a fluorine-containing monoamine aromatic organic compound.
  8. 如权利要求1-7中任一项所述的聚酰亚胺树脂的制备方法,其特征在于,所述含氟封端剂包括间二(三氟甲基)苯胺、4-(4'-氟苯基)苯甲腈、对三氟甲基苯胺、2,6-二氟-3-甲基苯胺、氰基乙酰对三氟甲基苯胺、4-甲基-2-(三氟甲基)苯胺、3-氟-2-(三氟甲基)苯胺、5-氟-2-三氟甲基苯胺、4-氟-2-硝基-5-(三氟甲基)-苯胺、2,2'-二(三氟甲基)二氨基联苯、三氟苯胺、N-乙基-2,3,5-三氟苯胺、2,2'-二(3,4,5-三氟苯基)-4,4'-联苯二胺、2,3,4-三氟苯乙酰胺、2,3,4-三氟-6-硝基苯胺中的任意一种。The method for preparing polyimide resin according to any one of claims 1-7, wherein the fluorine-containing end-capping agent comprises m-bis(trifluoromethyl)aniline, 4-(4'- Fluorophenyl)benzonitrile, p-trifluoromethylaniline, 2,6-difluoro-3-methylaniline, cyanoacetyl-p-trifluoromethylaniline, 4-methyl-2-(trifluoromethylaniline) ) aniline, 3-fluoro-2-(trifluoromethyl)aniline, 5-fluoro-2-trifluoromethylaniline, 4-fluoro-2-nitro-5-(trifluoromethyl)-aniline, 2 ,2'-bis(trifluoromethyl)diaminobiphenyl, trifluoroaniline, N-ethyl-2,3,5-trifluoroaniline, 2,2'-bis(3,4,5-trifluoroaniline) phenyl)-4,4'-benzidinediamine, any one of 2,3,4-trifluorophenylacetamide and 2,3,4-trifluoro-6-nitroaniline.
  9. 如权利要求1-8中任一项所述的聚酰亚胺树脂的制备方法,其特征在于,所述溶剂包括N,N-二甲基甲酰胺、N,N-二甲基乙酰胺、N-甲基吡咯烷酮、环己烷、甲基环己烷、四氢呋喃、异己烷、正庚烷、二氯甲烷、三氯乙烯、四氯化碳、环氧氯丙烷、甲基丙烯酸甲酯、二甲亚砜。The method for preparing polyimide resin according to any one of claims 1-8, wherein the solvent comprises N,N-dimethylformamide, N,N-dimethylacetamide, N-methylpyrrolidone, cyclohexane, methylcyclohexane, tetrahydrofuran, isohexane, n-heptane, dichloromethane, trichloroethylene, carbon tetrachloride, epichlorohydrin, methyl methacrylate, dichloromethane Methyl sulfoxide.
  10. 由权利要求权利要求1-9中任意一项所述的制备方法制备获得的聚酰亚胺树脂。The polyimide resin prepared by the preparation method described in any one of claims 1-9.
  11. 如权利要求权利要求10所述的聚酰亚胺树脂在薄膜中的用途。Use of the polyimide resin as claimed in claim 10 in a film.
  12. 一种薄膜,其特征在于,制备方法包括:选用权利要求1-9任意一项所述的聚酰亚胺树脂,在聚酰亚胺树脂中依次加入催化剂、脱水剂后涂覆在 基膜的至少一侧上。A film, characterized in that the preparation method comprises: selecting the polyimide resin according to any one of claims 1-9, adding a catalyst and a dehydrating agent to the polyimide resin in sequence, and then coating the base film on the base film. on at least one side.
  13. 如权利要求12所述的薄膜,其特征在于,所述催化剂包括哒嗪、嘧啶、砒嗪、酞嗪亦、1,10-菲咯啉。The film of claim 12, wherein the catalyst comprises pyridazine, pyrimidine, pyridine, phthalazine, and 1,10-phenanthroline.
  14. 如权利要求12所述的薄膜,其特征在于,所述催化剂与聚酰亚胺树脂溶液质量比为1:95-105。The film according to claim 12, wherein the mass ratio of the catalyst to the polyimide resin solution is 1:95-105.
  15. 如权利要求12所述的薄膜,其特征在于,所述基膜包括碳纳米纤维铜箔、碳纳米纤维银箔、碳纳米纤维铝箔、碳纳米纤维金箔。The film of claim 12, wherein the base film comprises carbon nanofiber copper foil, carbon nanofiber silver foil, carbon nanofiber aluminum foil, and carbon nanofiber gold foil.
PCT/CN2022/089436 2021-04-29 2022-04-27 Preparation method for polyimide resin and thin film thereof WO2022228449A1 (en)

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