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CN105860074A - Polyimide precursor solution, preparation method thereof and method of utilizing polyimide precursor solution to prepare polyimide thin film - Google Patents

Polyimide precursor solution, preparation method thereof and method of utilizing polyimide precursor solution to prepare polyimide thin film Download PDF

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CN105860074A
CN105860074A CN201610473006.XA CN201610473006A CN105860074A CN 105860074 A CN105860074 A CN 105860074A CN 201610473006 A CN201610473006 A CN 201610473006A CN 105860074 A CN105860074 A CN 105860074A
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tertiary amine
polyimide precursor
precursor solution
dianhydride
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刘长威
曲春艳
肖万宝
王德志
李洪峰
张杨
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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    • 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
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    • 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
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Abstract

一种聚酰亚胺前驱体溶液及其制备方法和利用其制备聚酰亚胺薄膜的方法,本发明涉及聚酰亚胺前驱体溶液及其制备方法和利用其制备聚酰亚胺薄膜的方法。本发明要解决现有聚酰亚胺前驱体‑聚酰胺酸水溶液的制备方法和结构组成难以实现在流延设备生产高表面质量和连续化不脆裂的聚酰亚胺薄膜的问题。一种聚酰亚胺前驱体溶液由叔胺、水性脱模剂、芳香二酐、芳香二胺、极性溶剂及水制成;制备方法:称取;在氮气气氛、一定温度及搅拌条件下,将水、极性溶剂和芳香二胺混合,将称取的芳香二酐加入到反应液中反应,在氮气气氛、一定温度及搅拌条件下,加入称取的叔胺和水性脱模剂反应,最后降温。制备聚酰亚胺薄膜:制备自支撑薄膜,然后固化、退火。

A kind of polyimide precursor solution and its preparation method and the method for using it to prepare polyimide film, the present invention relates to polyimide precursor solution and its preparation method and the method for using it to prepare polyimide film . The present invention solves the problem that the existing polyimide precursor-polyamic acid aqueous solution preparation method and structural composition are difficult to produce polyimide films with high surface quality and continuous non-brittle cracking in casting equipment. A polyimide precursor solution is made of tertiary amine, water-based release agent, aromatic dianhydride, aromatic diamine, polar solvent and water; preparation method: weighing; under nitrogen atmosphere, certain temperature and stirring conditions , mix water, polar solvent and aromatic diamine, add the weighed aromatic dianhydride into the reaction liquid for reaction, add the weighed tertiary amine and water-based release agent to react under nitrogen atmosphere, certain temperature and stirring conditions , and finally cool down. Preparation of polyimide film: Prepare a self-supporting film, then cure and anneal.

Description

一种聚酰亚胺前驱体溶液及其制备方法和利用其制备聚酰亚 胺薄膜的方法A kind of polyimide precursor solution and its preparation method and using it to prepare polyimide Amine film method

技术领域technical field

本发明涉及聚酰亚胺前驱体溶液及其制备方法和利用其制备聚酰亚胺薄膜的方法。The invention relates to a polyimide precursor solution, a preparation method thereof and a method for preparing a polyimide film using the same.

背景技术Background technique

聚酰亚胺是重复结构单元中含有酰亚胺环的芳杂环聚合物,它是迄今为止在工业领域应用的耐热等级最高的高分子材料,以其优异的综合性能在薄膜、树脂、纤维、分离膜等广泛地应用于航空航天、电子电气等领域。传统的聚酰亚胺通常由芳香族四甲酸酐和芳香族二胺为原料在非质子极性溶剂中,通过先形成聚酰胺酸,再亚胺化脱水形成聚酰亚胺。Polyimide is an aromatic heterocyclic polymer containing imide rings in repeating structural units. It is the highest heat-resistant polymer material used in the industrial field so far. With its excellent comprehensive performance, it can be used in films, resins, Fibers and separation membranes are widely used in aerospace, electronics and electrical fields. Traditional polyimides are usually made of aromatic tetracarboxylic anhydride and aromatic diamine in an aprotic polar solvent to form polyamic acid first, followed by imidization and dehydration to form polyimide.

现今随着微电子领域的发展,聚酰亚胺薄膜,尤其是无色聚酰亚胺,有希望作为柔性透明基底,替代ITO玻璃,在柔性可穿戴设备和柔性显示设备得到大量的应用。通常来说,聚酰亚胺前驱体溶液经历刮涂,流延成膜和热亚胺化等过程,最终收卷形成高质量薄膜。而采用极性溶剂,如N,N-二甲基乙酰胺,N,N-二甲基甲酰胺,N-甲基吡咯烷酮等,制备聚酰胺酸后,在流延挥发和热亚胺化过程中,都涉及到大量溶剂在烘道中挥发造成的废气和沉降后的废液污染。通常情况下,采用热风道可以一定程度的回收和再次提纯利用溶剂,但是现阶段技术难以实现100%的溶剂回收和100%的溶剂分离提纯。常规企业只能达到90%以上的回收,但是回收溶剂难以再制备高质量的聚合物;剩余部分的挥发份对大气和水源也会产生影响,从环保的角度已经成为看待聚酰亚胺薄膜为污染型的化工产品的重要因素,该问题已经成为聚酰亚胺制膜领域面临的重要难题。Nowadays, with the development of the microelectronics field, polyimide films, especially colorless polyimides, are expected to be used as flexible transparent substrates to replace ITO glass, and have been widely used in flexible wearable devices and flexible display devices. Generally speaking, the polyimide precursor solution undergoes processes such as doctor blade coating, casting film formation and thermal imidization, and finally winds up to form a high-quality film. And use polar solvents, such as N,N-dimethylacetamide, N,N-dimethylformamide, N-methylpyrrolidone, etc., after the preparation of polyamic acid, in the process of casting volatilization and thermal imidization Both involve the waste gas caused by volatilization of a large amount of solvent in the drying tunnel and the pollution of waste liquid after settlement. Under normal circumstances, the hot air duct can be used to recover and repurify the solvent to a certain extent, but it is difficult to achieve 100% solvent recovery and 100% solvent separation and purification in the current technology. Conventional enterprises can only achieve more than 90% recovery, but it is difficult to produce high-quality polymers by recycling solvents; the remaining volatile matter will also have an impact on the atmosphere and water sources. From the perspective of environmental protection, polyimide films have become the most important An important factor of polluting chemical products, this problem has become an important problem in the field of polyimide membrane production.

采用水作为聚酰胺酸的溶剂无疑会极大解决聚酰亚胺,尤其是聚酰亚胺薄膜制备过程中的困扰。在此方面,有文献报道,如《由水溶性聚酰胺酸制备聚酰亚胺》,绝缘材料1981(1):34-42,在极性溶剂中加入二酐/二胺形成聚酰胺酸后加入氨或有机胺进行中和,再加入水稀释得到溶液。但其溶液中依然引入大量的有机溶剂作为聚合的诱导剂。文献(High Performance Polymers,2003(15):269-279.)报道了先将二酐水解,再与二胺聚合形成聚酰胺酸在水中析出,将干物反复洗涤后在压力瓶中热环化得到聚酰亚胺粉末。过程极为繁复,对设备要求较高同时难以大批量制备。同时所得到聚酰胺酸不溶于水,难以应用在聚酰亚胺薄膜制备工艺。Using water as a solvent for polyamic acid will undoubtedly greatly solve the problems in the preparation of polyimide, especially polyimide film. In this regard, there are bibliographical reports, such as "preparation of polyimide by water-soluble polyamic acid", insulating material 1981 (1): 34-42, after adding dianhydride/diamine to form polyamic acid in polar solvent Add ammonia or organic amine for neutralization, then add water to dilute to obtain a solution. However, a large amount of organic solvent is still introduced into the solution as an inducer of polymerization. Literature (High Performance Polymers, 2003 (15): 269-279.) reported that the dianhydride was hydrolyzed earlier, and then polymerized with diamine to form polyamic acid, which was precipitated in water, and the dry matter was washed repeatedly and thermally cyclized in a pressure bottle to obtain Polyimide powder. The process is extremely complicated, requires high equipment and is difficult to prepare in large quantities. At the same time, the obtained polyamic acid is insoluble in water, so it is difficult to apply to the polyimide film preparation process.

类似的文献和专利报道中涉及到的水溶性聚酰胺酸溶液,均是对聚酰亚胺前驱体的结构研究,通过对结构的调整,评价实验室刮涂聚酰亚胺薄膜性能,如热性能、机械性能等。均没有涉及到由聚酰亚胺前驱体水溶液生产的流延涂覆形成自支撑膜、张力固化形成聚酰亚胺连续膜的报道。The water-soluble polyamic acid solutions involved in similar literature and patent reports are all researches on the structure of polyimide precursors. properties, mechanical properties, etc. There is no report about the self-supporting film formed by casting coating produced by polyimide precursor aqueous solution, and the continuous polyimide film formed by tension curing.

同时,文献和专利中涉及到的水溶性聚酰亚胺前驱体-聚酰胺酸溶液均采用一种金属盐或者胺盐催化形成聚酰亚胺前驱体,水性溶液进行加热形成自支撑前驱体膜的过程中,尚未亚胺化前水份基本挥发完(100℃),采用无机金属盐催化会导致残留到薄膜中;采用少量单一种类胺盐,会导致形成的自支撑膜表面留有催化剂脱出后剩余的空隙,一方面会影响最终形成聚酰亚胺薄膜的表面质量,另一方面空隙的形成也会对薄膜的材料性能造成影响。At the same time, the water-soluble polyimide precursor-polyamic acid solution involved in the literature and patents is catalyzed by a metal salt or amine salt to form a polyimide precursor, and the aqueous solution is heated to form a self-supporting precursor film. In the process of imidization, the water is basically volatilized (100°C), and the use of inorganic metal salts as catalysts will cause residues in the film; the use of a small amount of single-type amine salts will cause catalysts to come out from the surface of the formed self-supporting film On the one hand, the remaining voids will affect the surface quality of the final polyimide film, and on the other hand, the formation of voids will also affect the material properties of the film.

此外,通常选用N,N-二甲基乙酰胺(沸点164℃)作为溶剂形成聚酰亚胺前驱体溶液,流延脱出溶剂形成自支撑膜的温度在150℃到250℃之间,高分子量的聚酰亚胺前驱体-聚酰胺酸具有一定的薄膜强度,但是在亚胺化转化过程中(150℃-250℃),会面临分子量急剧减小,薄膜强度下降的危险,采用高沸点的N,N-二甲基乙酰胺作为溶剂,通过高温含溶剂一定程度的避免刚形成的自支撑膜变脆,降低了高温拉伸过程中的薄膜断裂的危险,提高了成形体的连续生产效率。而聚酰亚胺前驱体水溶液中水的沸点为100℃,流延涂布过程中脱除水份后的温度在60℃到120℃之间,低于亚胺化的温度,所以在形成无溶剂自支撑聚酰胺酸膜后,经历拉伸亚胺化反应过程中,由于分子量降低(150~250℃),有极大风险自支撑膜难以经受住系统牵引张力而发生断裂。In addition, N,N-dimethylacetamide (boiling point 164°C) is usually selected as a solvent to form a polyimide precursor solution, and the temperature for casting out the solvent to form a self-supporting film is between 150°C and 250°C. The polyimide precursor-polyamic acid has a certain film strength, but in the process of imidization conversion (150°C-250°C), it will face the danger of a sharp decrease in molecular weight and a decrease in film strength. N,N-Dimethylacetamide is used as a solvent to avoid the embrittlement of the newly formed self-supporting film to a certain extent by containing the solvent at high temperature, reducing the risk of film breakage during high temperature stretching, and improving the continuous production efficiency of the molded body . The boiling point of water in the polyimide precursor aqueous solution is 100°C, and the temperature after removing water in the casting coating process is between 60°C and 120°C, which is lower than the imidization temperature, so it is formed without After the solvent self-supporting polyamic acid film undergoes stretch imidization reaction, due to the decrease of molecular weight (150-250°C), there is a great risk that the self-supporting film cannot withstand the traction tension of the system and breaks.

从以上成形体的制备过程角度讲,并没有涉及到聚酰亚胺前驱体-聚酰胺酸水溶液的不同制备方法、不同催化剂类型,对聚酰亚胺流延膜的自支撑膜(聚酰胺酸膜)再经历固化炉的成膜难易度、以及与成形体聚酰亚胺薄膜的表面质量、强度的影响。From the perspective of the preparation process of the above molded body, the different preparation methods and different catalyst types of the polyimide precursor-polyamic acid aqueous solution are not involved, and the self-supporting film (polyamic acid) of the polyimide cast film is not involved. film) and then experience the difficulty of film formation in the curing oven, as well as the surface quality and strength of the formed polyimide film.

发明内容Contents of the invention

本发明要解决现有聚酰亚胺前驱体-聚酰胺酸水溶液的制备方法和结构组成难以实现在流延设备生产高表面质量和连续化不脆裂的聚酰亚胺薄膜的问题,而提供一种聚酰亚胺前驱体溶液及其制备方法和利用其制备聚酰亚胺薄膜的方法。The present invention will solve the problem that the existing polyimide precursor-polyamic acid aqueous solution preparation method and structural composition are difficult to realize the production of polyimide films with high surface quality and continuous non-brittle cracking in casting equipment, and provide A polyimide precursor solution, a preparation method thereof, and a method for preparing a polyimide film using the same.

一种聚酰亚胺前驱体溶液由叔胺、水性脱模剂、芳香二酐、芳香二胺、极性溶剂及水制成;A polyimide precursor solution is made of tertiary amine, aqueous release agent, aromatic dianhydride, aromatic diamine, polar solvent and water;

所述的芳香二胺与叔胺的摩尔比为1:(0.05~1.5);所述的芳香二胺与水性脱模剂的质量比为1:(0.01~1);所述的芳香二胺与芳香二酐的摩尔比为1:(0.97~1.03);所述的芳香二酐和芳香二胺的总质量与水的质量比为1:(2~10);所述的芳香二酐和芳香二胺的总质量与极性溶剂的质量比为1:(0~10);The molar ratio of the aromatic diamine to the tertiary amine is 1:(0.05~1.5); the mass ratio of the aromatic diamine to the aqueous release agent is 1:(0.01~1); the aromatic diamine The molar ratio to aromatic dianhydride is 1:(0.97~1.03); the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to water is 1:(2~10); the aromatic dianhydride and The mass ratio of the total mass of aromatic diamine to the polar solvent is 1:(0~10);

所述的芳香二胺为4,4′-二氨基二苯醚、4,4′-二氨基二苯甲烷、二(3-氨基苯氧基)二苯甲酮、对苯二胺、间苯二胺和4,4′-二氨基二苯砜中的一种或其中几种的混合物;The aromatic diamines are 4,4'-diaminodiphenyl ether, 4,4'-diaminodiphenylmethane, bis(3-aminophenoxy)benzophenone, p-phenylenediamine, m-phenylenediamine One or a mixture of diamines and 4,4'-diaminodiphenylsulfone;

所述的叔胺为低沸点叔胺或低沸点叔胺与高沸点叔胺的混合物,所述的低沸点叔胺与高沸点叔胺的摩尔比例为1:(0.01~100);所述的低沸点叔胺为沸点在150℃以下,且低沸点叔胺的分子量为80g/mol~250g/mol;所述的高沸点叔胺为沸点在150℃~295℃的叔胺;The tertiary amine is a low-boiling tertiary amine or a mixture of a low-boiling tertiary amine and a high-boiling tertiary amine, and the molar ratio of the low-boiling tertiary amine to the high-boiling tertiary amine is 1:(0.01-100); the The low-boiling point tertiary amine has a boiling point below 150°C, and the molecular weight of the low-boiling point tertiary amine is 80g/mol-250g/mol; the high-boiling point tertiary amine is a tertiary amine with a boiling point between 150°C-295°C;

所述的极性溶剂为N,N-二甲基乙酰胺、N,N-二甲基甲酰胺、乙二醇和二甲基亚砜中的一种或其中几种的混合物;The polar solvent is one of N,N-dimethylacetamide, N,N-dimethylformamide, ethylene glycol and dimethyl sulfoxide or a mixture of several of them;

当所述的芳香二酐为3,3,4′,4′-二苯醚四羧酸二酐、3,3,4′,4′-二砜基四羧酸二酐或3,3,4′,4′-二苯甲酮四羧酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride is 3,3,4',4'-diphenyl ether tetracarboxylic dianhydride, 3,3,4',4'-disulfone tetracarboxylic dianhydride or 3,3, 4',4'-benzophenone tetracarboxylic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is:

所述的R1为-O-或 The R 1 is -O- or

所述的R2 The R2 is

当所述的芳香二酐为3,3,4′,4′-联苯四羧酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride is 3,3,4′,4′-biphenyltetracarboxylic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is:

所述的R3 The R3 is

当所述的芳香二酐为均苯四甲酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride is pyromellitic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is:

所述的R4 The R 4 is

一种聚酰亚胺前驱体溶液的制备方法是按以下步骤进行:A kind of preparation method of polyimide precursor solution is to carry out according to the following steps:

一、取叔胺、水性脱模剂、芳香二酐、芳香二胺、极性溶剂及水;1. Take tertiary amine, water-based release agent, aromatic dianhydride, aromatic diamine, polar solvent and water;

所述的芳香二胺与叔胺的摩尔比为1:(0.05~1.5);所述的芳香二胺与水性脱模剂的质量比为1:(0.01~1);所述的芳香二胺与芳香二酐的摩尔比为1:(0.97~1.03);所述的芳香二酐和芳香二胺的总质量与水的质量比为1:(2~10);所述的芳香二酐和芳香二胺的总质量与极性溶剂的质量比为1:(0~10);The molar ratio of the aromatic diamine to the tertiary amine is 1:(0.05~1.5); the mass ratio of the aromatic diamine to the aqueous release agent is 1:(0.01~1); the aromatic diamine The molar ratio to aromatic dianhydride is 1:(0.97~1.03); the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to water is 1:(2~10); the aromatic dianhydride and The mass ratio of the total mass of aromatic diamine to the polar solvent is 1:(0~10);

二、在氮气气氛、温度为2℃~10℃及搅拌条件下,向三颈瓶中加入步骤一中称取的水和极性溶剂,然后加入步骤一中称取的芳香二胺,得到反应液,将步骤一中称取的芳香二酐按质量平均分三次加入到反应液中,反应1h~5h,然后将反应液升温至20℃~60℃,在氮气气氛、温度为20℃~60℃及搅拌条件下,向反应液中加入步骤一中称取的叔胺和水性脱模剂,搅拌反应3h~5h,最后将反应液温度降低至2℃~10℃,静置1h~10h,得到聚酰亚胺前驱体溶液;2. In a nitrogen atmosphere, at a temperature of 2°C to 10°C and under stirring conditions, add the water and polar solvent weighed in step 1 to the three-necked flask, and then add the aromatic diamine weighed in step 1 to obtain the reaction solution, the aromatic dianhydride weighed in step 1 was added to the reaction solution in three equal parts by mass, reacted for 1h to 5h, and then the reaction solution was heated to 20°C to 60°C, in a nitrogen atmosphere, the temperature was 20°C to 60°C ℃ and under stirring conditions, add the tertiary amine and water-based release agent weighed in step 1 to the reaction solution, stir and react for 3h to 5h, and finally reduce the temperature of the reaction solution to 2℃~10℃, and let it stand for 1h~10h. Obtain polyimide precursor solution;

步骤一中所述的芳香二胺为4,4′-二氨基二苯醚、4,4′-二氨基二苯甲烷、二(3-氨基苯氧基)二苯甲酮、对苯二胺、间苯二胺和4,4′-二氨基二苯砜中的一种或其中几种的混合物;The aromatic diamine described in step 1 is 4,4'-diaminodiphenyl ether, 4,4'-diaminodiphenylmethane, bis(3-aminophenoxy)benzophenone, p-phenylenediamine , m-phenylenediamine and 4,4'-diaminodiphenyl sulfone or a mixture of several of them;

步骤一中所述的叔胺为低沸点叔胺或低沸点叔胺与高沸点叔胺的混合物,所述的低沸点叔胺与高沸点叔胺的摩尔比例为1:(0.01~100);所述的低沸点叔胺为沸点在150℃以下,且低沸点叔胺的分子量为80g/mol~250g/mol;所述的高沸点叔胺为沸点在150℃~295℃的叔胺;The tertiary amine described in step 1 is a low-boiling tertiary amine or a mixture of a low-boiling tertiary amine and a high-boiling tertiary amine, and the molar ratio of the low-boiling tertiary amine to the high-boiling tertiary amine is 1:(0.01~100); The low-boiling tertiary amine has a boiling point below 150°C, and the molecular weight of the low-boiling tertiary amine is 80g/mol-250g/mol; the high-boiling tertiary amine is a tertiary amine with a boiling point of 150°C-295°C;

步骤一中所述的极性溶剂为N,N-二甲基乙酰胺、N,N-二甲基甲酰胺、乙二醇和二甲基亚砜中的一种或其中几种的混合物;The polar solvent described in step 1 is one or a mixture of several of N,N-dimethylacetamide, N,N-dimethylformamide, ethylene glycol and dimethyl sulfoxide;

当步骤一中所述的芳香二酐为3,3,4′,4′-二苯醚四羧酸二酐、3,3,4′,4′-二砜基四羧酸二酐或3,3,4′,4′-二苯甲酮四羧酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride described in step 1 is 3,3,4',4'-diphenyl ether tetracarboxylic dianhydride, 3,3,4',4'-disulfone tetracarboxylic dianhydride or 3 , 3,4',4'-benzophenone tetracarboxylic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is:

所述的R1为-O-或 The R 1 is -O- or

所述的R2 The R2 is

当步骤一中所述的芳香二酐为3,3,4′,4′-联苯四羧酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride described in step 1 is 3,3,4′,4′-biphenyltetracarboxylic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is:

所述的R3 The R3 is

当步骤一中所述的芳香二酐为均苯四甲酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride described in step 1 is pyromellitic dianhydride, the repeating unit of polyamic acid in the described polyimide precursor solution is:

所述的R4 The R 4 is

利用一种聚酰亚胺前驱体溶液制备聚酰亚胺薄膜的方法是按以下步骤进行:The method that utilizes a kind of polyimide precursor solution to prepare polyimide film is to carry out as follows:

一、将聚酰亚胺前驱体溶液过滤并脱气,沿着T型狭缝流延到不锈钢制转鼓上,然后在温度为60℃~180℃下,干燥1min~50min,得到自支撑薄膜;1. Filter and degas the polyimide precursor solution, cast it on a stainless steel drum along the T-shaped slit, and then dry it at a temperature of 60 ° C to 180 ° C for 1 min to 50 min to obtain a self-supporting film ;

二、将自支撑薄膜从不锈钢制转鼓上剥离并置于固化炉中固化,首先在温度为150℃~200℃的条件下,加热1min~60min,再在温度为200℃~250℃的条件下,加热1min~60min,然后在温度为250℃~450℃的条件下,加热1min~60min,最后在温度为290℃~310℃的条件下,退火处理约1min~20min,得到聚酰亚胺薄膜;2. Peel the self-supporting film from the stainless steel drum and place it in a curing furnace for curing. First, heat it for 1min to 60min at a temperature of 150°C to 200°C, and then heat it at a temperature of 200°C to 250°C. , heating for 1min to 60min, then heating for 1min to 60min at a temperature of 250°C to 450°C, and finally annealing for about 1min to 20min at a temperature of 290°C to 310°C to obtain polyimide film;

且固化过程中利用夹具夹持自支撑薄膜,使得自支撑薄膜固化前后纵向长度变化百分率为5%~20%,横向长度变化百分率为10%~80%。And during the curing process, the self-supporting film is clamped by a clamp, so that the percentage change of the longitudinal length of the self-supporting film before and after curing is 5%-20%, and the percentage change of the transverse length is 10%-80%.

本发明的有益效果是:本发明提供的一种聚酰亚胺前驱体溶液及其制备方法和利用其制备聚酰亚胺薄膜的方法,可以解决现有聚酰亚胺前驱体-聚酰胺酸水溶液的制备方法和结构组成难以实现在流延设备生产高表面质量和连续化不脆裂的聚酰亚胺薄膜的问题。根据聚酰亚胺前驱体溶液的制备方法,采用了低比例高沸点极性溶剂、多种沸点叔胺复合物的组合。The beneficial effect of the present invention is: a kind of polyimide precursor solution provided by the present invention and its preparation method and the method for using it to prepare polyimide film can solve the problem of existing polyimide precursor-polyamic acid The preparation method and structural composition of the aqueous solution are difficult to realize the problem of producing high surface quality and continuous non-brittle polyimide films in casting equipment. According to the preparation method of the polyimide precursor solution, a combination of a low-proportion high-boiling-point polar solvent and various boiling-point tertiary amine compounds is used.

一方面,利用高沸点极性溶剂(如N,N-二甲基乙酰胺、N,N-二甲基甲酰胺等)与水的组合,提高溶剂整体沸点,避免形成的自支撑聚酰亚胺前驱体薄膜含溶剂量过少(少于20%)和沸点低,虽然自支撑膜依然经历高温亚胺化(有拉伸作用或无拉伸作用)过程(150℃-250℃)中会出现分子量下降和强度下降的情况,但是含溶剂量的提升和沸点提高,极大程度提高了初始亚胺化(150℃-200℃)的伸长率和柔韧性,避免了在高温由于外部载荷导致的薄膜断裂的危险,影响薄膜连续化操作。On the one hand, use the combination of high boiling point polar solvents (such as N,N-dimethylacetamide, N,N-dimethylformamide, etc.) and water to increase the overall boiling point of the solvent and avoid the formation of self-supporting polyimide The amine precursor film contains too little solvent (less than 20%) and has a low boiling point. Although the self-supporting film still undergoes high-temperature imidization (with or without stretching) process (150°C-250°C), it will There is a decrease in molecular weight and a decrease in strength, but the increase in solvent content and the increase in boiling point greatly improve the elongation and flexibility of the initial imidization (150°C-200°C), avoiding the high temperature due to external load The resulting danger of film breakage affects the continuous operation of the film.

另一方面,聚酰亚胺前驱体溶液制备方法采用了多种沸点叔胺复合物,从而在流延脱出溶剂形成自支撑膜时,仍含有多种沸点叔胺在前驱体中。在亚胺化程序中将自支撑膜倒入固化炉进行处理,尤其是对于连续化的处理自支撑膜的热亚胺化,需要施加一定的轴向外部载荷提供牵引,在水分基本挥发后(<150℃),常用单一叔胺类也面临在150℃下挥发的风险,难以作为液态残留提升弥补初始亚胺化后(150℃-250℃)低强度、低伸长率。采用多种叔胺提供多种脱除温度和沸点,实现在大于150℃时仍保留有一定液态残留。并且和高沸点溶剂组合的方式复合使用,能够进一步确保在亚胺化初始温度条件下的薄膜持续伸长和膨胀系数,极大避免了在亚胺化初始的薄膜破坏,尤其是受到牵引力作用下薄膜的破坏,从而节省了固化炉降温、重新穿膜、升温的电力和时间成本。On the other hand, the polyimide precursor solution preparation method uses a variety of boiling point tertiary amine complexes, so that when the solvent is cast out to form a self-supporting film, the precursor still contains a variety of boiling point tertiary amines. In the imidization process, the self-supporting film is poured into the curing furnace for processing, especially for the thermal imidization of the self-supporting film for continuous treatment, it is necessary to apply a certain axial external load to provide traction. After the water is basically volatilized ( <150°C), commonly used single tertiary amines also face the risk of volatilization at 150°C, and it is difficult to improve the low strength and low elongation after initial imidization (150°C-250°C) as a liquid residue. A variety of tertiary amines are used to provide a variety of removal temperatures and boiling points to achieve a certain liquid residue at temperatures above 150°C. And combined with high boiling point solvents, it can further ensure the continuous elongation and expansion coefficient of the film at the initial temperature of imidization, and greatly avoid the film damage at the initial imidization, especially under the action of traction The destruction of the film saves the cost of electricity and time for cooling the curing furnace, re-piercing the film, and heating up.

出乎意料的是,多种叔胺的复合使用,不仅有利于提升薄膜各阶段成型强度,同时还提高了薄膜的表面质量和降低了缺陷。由于低沸点的单一叔胺和水在挥发后,聚酰亚胺前驱体面临快速亚胺化和溶剂、催化剂脱出的双重压力,会严重导致的薄膜表面平整度差、表面有挥发脱出留下的气孔、亚胺化短时脱除大量水留下的闭孔等,对薄膜的表面质量有很大影响。采用低沸点和高沸点叔胺并用的方式,出乎意料的获得了不同亚胺化条件下持续的挥发效果,使聚酰亚胺薄膜形成过程中不依靠外力而提供自流平的效果,极大的解决了薄膜的表面质量问题。尤其是对于连续化薄膜的热亚胺化操作,不仅减少了褶皱和空隙的出现,薄膜平整度也得到增强。且本发明制备的聚酰亚胺前驱体溶液还可用于形成聚酰亚胺纤维。Unexpectedly, the combined use of various tertiary amines not only helps to improve the forming strength of the film at each stage, but also improves the surface quality of the film and reduces defects. After the single tertiary amine with a low boiling point and water volatilize, the polyimide precursor faces the double pressure of rapid imidization and solvent and catalyst detachment, which will seriously cause poor surface roughness of the film and surface left by volatilization. Pores, closed pores left by removing a large amount of water in a short period of imidization, etc., have a great influence on the surface quality of the film. Using the combination of low-boiling point and high-boiling point tertiary amines, unexpectedly obtained the continuous volatilization effect under different imidization conditions, so that the polyimide film formation process does not rely on external forces to provide self-leveling effect, greatly It solves the surface quality problem of the film. Especially for the thermal imidization operation of continuous film, not only the occurrence of wrinkles and voids is reduced, but also the flatness of the film is enhanced. And the polyimide precursor solution prepared by the present invention can also be used to form polyimide fibers.

本发明用于一种聚酰亚胺前驱体溶液及其制备方法和利用其制备聚酰亚胺薄膜的方法。The invention is used for a polyimide precursor solution, a preparation method thereof and a method for preparing a polyimide film by using the same.

附图说明Description of drawings

图1为实施例四制备的聚酰亚胺薄膜照片;Fig. 1 is the polyimide film photo that embodiment four prepares;

图2为对比实验一制备的聚酰亚胺薄膜照片。Figure 2 is a photo of the polyimide film prepared in Comparative Experiment 1.

具体实施方式detailed description

具体实施方式一:本实施方式的一种聚酰亚胺前驱体溶液由叔胺、水性脱模剂、芳香二酐、芳香二胺、极性溶剂及水制成;Embodiment 1: A polyimide precursor solution in this embodiment is made of tertiary amine, aqueous release agent, aromatic dianhydride, aromatic diamine, polar solvent and water;

所述的芳香二胺与叔胺的摩尔比为1:(0.05~1.5);所述的芳香二胺与水性脱模剂的质量比为1:(0.01~1);所述的芳香二胺与芳香二酐的摩尔比为1:(0.97~1.03);所述的芳香二酐和芳香二胺的总质量与水的质量比为1:(2~10);所述的芳香二酐和芳香二胺的总质量与极性溶剂的质量比为1:(0~10);The molar ratio of the aromatic diamine to the tertiary amine is 1:(0.05~1.5); the mass ratio of the aromatic diamine to the aqueous release agent is 1:(0.01~1); the aromatic diamine The molar ratio to aromatic dianhydride is 1:(0.97~1.03); the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to water is 1:(2~10); the aromatic dianhydride and The mass ratio of the total mass of aromatic diamine to the polar solvent is 1:(0~10);

所述的芳香二胺为4,4′-二氨基二苯醚、4,4′-二氨基二苯甲烷、二(3-氨基苯氧基)二苯甲酮、对苯二胺、间苯二胺和4,4′-二氨基二苯砜中的一种或其中几种的混合物;The aromatic diamines are 4,4'-diaminodiphenyl ether, 4,4'-diaminodiphenylmethane, bis(3-aminophenoxy)benzophenone, p-phenylenediamine, m-phenylenediamine One or a mixture of diamines and 4,4'-diaminodiphenylsulfone;

所述的叔胺为低沸点叔胺或低沸点叔胺与高沸点叔胺的混合物,所述的低沸点叔胺与高沸点叔胺的摩尔比例为1:(0.01~100);所述的低沸点叔胺为沸点在150℃以下,且低沸点叔胺的分子量为80g/mol~250g/mol;所述的高沸点叔胺为沸点在150℃~295℃的叔胺;The tertiary amine is a low-boiling tertiary amine or a mixture of a low-boiling tertiary amine and a high-boiling tertiary amine, and the molar ratio of the low-boiling tertiary amine to the high-boiling tertiary amine is 1:(0.01-100); the The low-boiling point tertiary amine has a boiling point below 150°C, and the molecular weight of the low-boiling point tertiary amine is 80g/mol-250g/mol; the high-boiling point tertiary amine is a tertiary amine with a boiling point between 150°C-295°C;

所述的极性溶剂为N,N-二甲基乙酰胺、N,N-二甲基甲酰胺、乙二醇和二甲基亚砜中的一种或其中几种的混合物;The polar solvent is one of N,N-dimethylacetamide, N,N-dimethylformamide, ethylene glycol and dimethyl sulfoxide or a mixture of several of them;

当所述的芳香二酐为3,3,4′,4′-二苯醚四羧酸二酐、3,3,4′,4′-二砜基四羧酸二酐或3,3,4′,4′-二苯甲酮四羧酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride is 3,3,4',4'-diphenyl ether tetracarboxylic dianhydride, 3,3,4',4'-disulfone tetracarboxylic dianhydride or 3,3, 4',4'-benzophenone tetracarboxylic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is:

所述的R1为-O-或 The R 1 is -O- or

所述的R2 The R2 is

当所述的芳香二酐为3,3,4′,4′-联苯四羧酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride is 3,3,4′,4′-biphenyltetracarboxylic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is:

所述的R3 The R3 is

当所述的芳香二酐为均苯四甲酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride is pyromellitic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is:

所述的R4 The R 4 is

本实施方式的有益效果是:本实施方式提供的一种聚酰亚胺前驱体溶液及其制备方法和利用其制备聚酰亚胺薄膜的方法,可以解决现有聚酰亚胺前驱体-聚酰胺酸水溶液的制备方法和结构组成难以实现在流延设备生产高表面质量和连续化不脆裂的聚酰亚胺薄膜的问题。根据聚酰亚胺前驱体溶液的制备方法,采用了低比例高沸点极性溶剂、多种沸点叔胺复合物的组合。The beneficial effect of this embodiment is: a kind of polyimide precursor solution provided by this embodiment and its preparation method and the method for using it to prepare polyimide film can solve the problem of existing polyimide precursor - polyimide The preparation method and structural composition of the amic acid aqueous solution are difficult to realize the problem of producing high surface quality and continuous non-brittle polyimide films in tape casting equipment. According to the preparation method of the polyimide precursor solution, a combination of a low-proportion high-boiling-point polar solvent and various boiling-point tertiary amine compounds is used.

一方面,利用高沸点极性溶剂(如N,N-二甲基乙酰胺、N,N-二甲基甲酰胺等)与水的组合,提高溶剂整体沸点,避免形成的自支撑聚酰亚胺前驱体薄膜含溶剂量过少(少于20%)和沸点低,虽然自支撑膜依然经历高温亚胺化(有拉伸作用或无拉伸作用)过程(150℃-250℃)中会出现分子量下降和强度下降的情况,但是含溶剂量的提升和沸点提高,极大程度提高了初始亚胺化(150℃-200℃)的伸长率和柔韧性,避免了在高温由于外部载荷导致的薄膜断裂的危险,影响薄膜连续化操作。On the one hand, use the combination of high boiling point polar solvents (such as N,N-dimethylacetamide, N,N-dimethylformamide, etc.) and water to increase the overall boiling point of the solvent and avoid the formation of self-supporting polyimide The amine precursor film contains too little solvent (less than 20%) and has a low boiling point. Although the self-supporting film still undergoes high-temperature imidization (with or without stretching) process (150°C-250°C), it will There is a decrease in molecular weight and a decrease in strength, but the increase in solvent content and the increase in boiling point greatly improve the elongation and flexibility of the initial imidization (150°C-200°C), avoiding the high temperature due to external load The resulting danger of film breakage affects the continuous operation of the film.

另一方面,聚酰亚胺前驱体溶液制备方法采用了多种沸点叔胺复合物,从而在流延脱出溶剂形成自支撑膜时,仍含有多种沸点叔胺在前驱体中。在亚胺化程序中将自支撑膜倒入固化炉进行处理,尤其是对于连续化的处理自支撑膜的热亚胺化,需要施加一定的轴向外部载荷提供牵引,在水分基本挥发后(<150℃),常用单一叔胺类也面临在150℃下挥发的风险,难以作为液态残留提升弥补初始亚胺化后(150℃-250℃)低强度、低伸长率。采用多种叔胺提供多种脱除温度和沸点,实现在大于150℃时仍保留有一定液态残留。并且和高沸点溶剂组合的方式复合使用,能够进一步确保在亚胺化初始温度条件下的薄膜持续伸长和膨胀系数,极大避免了在亚胺化初始的薄膜破坏,尤其是受到牵引力作用下薄膜的破坏,从而节省了固化炉降温、重新穿膜、升温的电力和时间成本。On the other hand, the polyimide precursor solution preparation method uses a variety of boiling point tertiary amine complexes, so that when the solvent is cast out to form a self-supporting film, the precursor still contains a variety of boiling point tertiary amines. In the imidization process, the self-supporting film is poured into the curing furnace for processing, especially for the thermal imidization of the self-supporting film for continuous treatment, it is necessary to apply a certain axial external load to provide traction. After the water is basically volatilized ( <150°C), commonly used single tertiary amines also face the risk of volatilization at 150°C, and it is difficult to improve the low strength and low elongation after initial imidization (150°C-250°C) as a liquid residue. A variety of tertiary amines are used to provide a variety of removal temperatures and boiling points to achieve a certain liquid residue at temperatures above 150°C. And combined with high boiling point solvents, it can further ensure the continuous elongation and expansion coefficient of the film at the initial temperature of imidization, and greatly avoid the film damage at the initial imidization, especially under the action of traction The destruction of the film saves the cost of electricity and time for cooling the curing furnace, re-piercing the film, and heating up.

出乎意料的是,多种叔胺的复合使用,不仅有利于提升薄膜各阶段成型强度,同时还提高了薄膜的表面质量和降低了缺陷。由于低沸点的单一叔胺和水在挥发后,聚酰亚胺前驱体面临快速亚胺化和溶剂、催化剂脱出的双重压力,会严重导致的薄膜表面平整度差、表面有挥发脱出留下的气孔、亚胺化短时脱除大量水留下的闭孔等,对薄膜的表面质量有很大影响。采用低沸点和高沸点叔胺并用的方式,出乎意料的获得了不同亚胺化条件下持续的挥发效果,使聚酰亚胺薄膜形成过程中不依靠外力而提供自流平的效果,极大的解决了薄膜的表面质量问题。尤其是对于连续化薄膜的热亚胺化操作,不仅减少了褶皱和空隙的出现,薄膜平整度也得到增强。且具体实施方式制备的聚酰亚胺前驱体溶液还可用于形成聚酰亚胺纤维。Unexpectedly, the combined use of various tertiary amines not only helps to improve the forming strength of the film at each stage, but also improves the surface quality of the film and reduces defects. After the single tertiary amine with a low boiling point and water volatilize, the polyimide precursor faces the double pressure of rapid imidization and solvent and catalyst detachment, which will seriously cause poor surface roughness of the film and surface left by volatilization. Pores, closed pores left by removing a large amount of water in a short period of imidization, etc., have a great influence on the surface quality of the film. Using the combination of low-boiling point and high-boiling point tertiary amines, unexpectedly obtained the continuous volatilization effect under different imidization conditions, so that the polyimide film formation process does not rely on external forces to provide self-leveling effect, greatly It solves the surface quality problem of the film. Especially for the thermal imidization operation of continuous film, not only the occurrence of wrinkles and voids is reduced, but also the flatness of the film is enhanced. And the polyimide precursor solution prepared in the specific embodiment can also be used to form polyimide fibers.

具体实施方式二:本实施方式与具体实施方式一不同的是:所述的低沸点叔胺为三乙基胺、十二烷基二甲基叔胺、二乙醇单异丙醇胺和甲基吡啶中的一种或其中几种的混合物。其它与具体实施方式一相同。Specific embodiment two: the difference between this embodiment and specific embodiment one is: the low boiling point tertiary amine is triethylamine, dodecyl dimethyl tertiary amine, diethanol monoisopropanolamine and methyl One or a mixture of pyridines. Others are the same as in the first embodiment.

具体实施方式三:本实施方式与具体实施方式一或二之一不同的是:所述的高沸点叔胺为三正丁胺、三异丙醇胺和二甲胺基甲酰氯中的一种或其中几种的混合物。其它与具体实施方式一或二相同。Specific embodiment three: the difference between this embodiment and specific embodiment one or two is that: the high-boiling point tertiary amine is one of tri-n-butylamine, triisopropanolamine and dimethylcarbamoyl chloride or a mixture of several of them. Others are the same as in the first or second embodiment.

具体实施方式四:本实施方式与具体实施方式一至三之一不同的是:所述的水性脱模剂为在温度小于100℃的条件下能与水互溶,且不析出的脱模剂或离型剂。其它与具体实施方式一至三相同。Embodiment 4: This embodiment differs from Embodiments 1 to 3 in that the water-based release agent is a release agent or release agent that is miscible with water and does not precipitate when the temperature is less than 100°C. Formulations. Others are the same as the specific embodiments 1 to 3.

具体实施方式五:本实施方式与具体实施方式一至四之一不同的是:所述的水性脱模剂为RPLUS S02-004、Sepaluck RA715W、Sepaluck RA733W、NS-100或SepaluckRA780W。其它与具体实施方式一至四相同。Embodiment 5: This embodiment differs from Embodiment 1 to Embodiment 4 in that the water-based release agent is RPLUS S02-004, Sepaluck RA715W, Sepaluck RA733W, NS-100 or SepaluckRA780W. Others are the same as the specific embodiments 1 to 4.

RPLUS S02-004为德国克鲁勃公司生产;Sepaluck RA715W、Sepaluck RA733W、NS-100和Sepaluck RA780W为日本山一化学公司生产。RPLUS S02-004 is produced by Klüber Company in Germany; Sepaluck RA715W, Sepaluck RA733W, NS-100 and Sepaluck RA780W are produced by Yamaichi Chemical Company in Japan.

具体实施方式六:本实施方式与具体实施方式一至五之一不同的是:所述的芳香二酐和芳香二胺的总质量与极性溶剂的质量比为1:(0~1.5);所述的低沸点叔胺与高沸点叔胺的摩尔比例为1:(0.5~100)。其它与具体实施方式一至五相同。Specific embodiment six: the difference between this embodiment and one of specific embodiments one to five is that: the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to the polar solvent is 1: (0-1.5); The molar ratio of the low-boiling tertiary amine to the high-boiling tertiary amine is 1:(0.5-100). Others are the same as those in Embodiments 1 to 5.

本具体实施方式芳香二酐和芳香二胺的总质量与极性溶剂的质量比能提供低溶剂负担且保持较好效果。In this specific embodiment, the mass ratio of the total mass of aromatic dianhydride and aromatic diamine to the polar solvent can provide low solvent burden and maintain a good effect.

具体实施方式七:本实施方式所述的一种聚酰亚胺前驱体溶液的制备方法是按以下步骤进行:Specific embodiment seven: the preparation method of a kind of polyimide precursor solution described in this embodiment is to carry out according to the following steps:

一、取叔胺、水性脱模剂、芳香二酐、芳香二胺、极性溶剂及水;1. Take tertiary amine, water-based release agent, aromatic dianhydride, aromatic diamine, polar solvent and water;

所述的芳香二胺与叔胺的摩尔比为1:(0.05~1.5);所述的芳香二胺与水性脱模剂的质量比为1:(0.01~1);所述的芳香二胺与芳香二酐的摩尔比为1:(0.97~1.03);所述的芳香二酐和芳香二胺的总质量与水的质量比为1:(2~10);所述的芳香二酐和芳香二胺的总质量与极性溶剂的质量比为1:(0~10);The molar ratio of the aromatic diamine to the tertiary amine is 1:(0.05~1.5); the mass ratio of the aromatic diamine to the aqueous release agent is 1:(0.01~1); the aromatic diamine The molar ratio to aromatic dianhydride is 1:(0.97~1.03); the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to water is 1:(2~10); the aromatic dianhydride and The mass ratio of the total mass of aromatic diamine to the polar solvent is 1:(0~10);

二、在氮气气氛、温度为2℃~10℃及搅拌条件下,向三颈瓶中加入步骤一中称取的水和极性溶剂,然后加入步骤一中称取的芳香二胺,得到反应液,将步骤一中称取的芳香二酐按质量平均分三次加入到反应液中,反应1h~5h,然后将反应液升温至20℃~60℃,在氮气气氛、温度为20℃~60℃及搅拌条件下,向反应液中加入步骤一中称取的叔胺和水性脱模剂,搅拌反应3h~5h,最后将反应液温度降低至2℃~10℃,静置1h~10h,得到聚酰亚胺前驱体溶液;2. In a nitrogen atmosphere, at a temperature of 2°C to 10°C and under stirring conditions, add the water and polar solvent weighed in step 1 to the three-necked flask, and then add the aromatic diamine weighed in step 1 to obtain the reaction solution, the aromatic dianhydride weighed in step 1 was added to the reaction solution in three equal parts by mass, reacted for 1h to 5h, and then the reaction solution was heated to 20°C to 60°C, in a nitrogen atmosphere, the temperature was 20°C to 60°C ℃ and under stirring conditions, add the tertiary amine and water-based release agent weighed in step 1 to the reaction solution, stir and react for 3h to 5h, and finally reduce the temperature of the reaction solution to 2℃~10℃, and let it stand for 1h~10h. Obtain polyimide precursor solution;

步骤一中所述的芳香二胺为4,4′-二氨基二苯醚、4,4′-二氨基二苯甲烷、二(3-氨基苯氧基)二苯甲酮、对苯二胺、间苯二胺和4,4′-二氨基二苯砜中的一种或其中几种的混合物;The aromatic diamine described in step 1 is 4,4'-diaminodiphenyl ether, 4,4'-diaminodiphenylmethane, bis(3-aminophenoxy)benzophenone, p-phenylenediamine , m-phenylenediamine and 4,4'-diaminodiphenyl sulfone or a mixture of several of them;

步骤一中所述的叔胺为低沸点叔胺或低沸点叔胺与高沸点叔胺的混合物,所述的低沸点叔胺与高沸点叔胺的摩尔比例为1:(0.01~100);所述的低沸点叔胺为沸点在150℃以下,且低沸点叔胺的分子量为80g/mol~250g/mol;所述的高沸点叔胺为沸点在150℃~295℃的叔胺;The tertiary amine described in step 1 is a low-boiling tertiary amine or a mixture of a low-boiling tertiary amine and a high-boiling tertiary amine, and the molar ratio of the low-boiling tertiary amine to the high-boiling tertiary amine is 1:(0.01~100); The low-boiling tertiary amine has a boiling point below 150°C, and the molecular weight of the low-boiling tertiary amine is 80g/mol-250g/mol; the high-boiling tertiary amine is a tertiary amine with a boiling point of 150°C-295°C;

步骤一中所述的极性溶剂为N,N-二甲基乙酰胺、N,N-二甲基甲酰胺、乙二醇和二甲基亚砜中的一种或其中几种的混合物;The polar solvent described in step 1 is one or a mixture of several of N,N-dimethylacetamide, N,N-dimethylformamide, ethylene glycol and dimethyl sulfoxide;

当步骤一中所述的芳香二酐为3,3,4′,4′-二苯醚四羧酸二酐、3,3,4′,4′-二砜基四羧酸二酐或3,3,4′,4′-二苯甲酮四羧酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride described in step 1 is 3,3,4',4'-diphenyl ether tetracarboxylic dianhydride, 3,3,4',4'-disulfone tetracarboxylic dianhydride or 3 , 3,4',4'-benzophenone tetracarboxylic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is:

所述的R1为-O-或 The R 1 is -O- or

所述的R2 The R2 is

当步骤一中所述的芳香二酐为3,3,4′,4′-联苯四羧酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride described in step 1 is 3,3,4′,4′-biphenyltetracarboxylic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is:

所述的R3 The R3 is

当步骤一中所述的芳香二酐为均苯四甲酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride described in step 1 is pyromellitic dianhydride, the repeating unit of polyamic acid in the described polyimide precursor solution is:

所述的R4 The R 4 is

具体实施方式八:本实施方式与具体实施方式七不同的是:步骤一中所述的低沸点叔胺为三乙基胺、十二烷基二甲基叔胺、二乙醇单异丙醇胺和甲基吡啶中的一种或其中几种的混合物。其它与具体实施方式七相同。Embodiment 8: The difference between this embodiment and Embodiment 7 is that the low-boiling tertiary amine described in step 1 is triethylamine, dodecyldimethyl tertiary amine, diethanol monoisopropanolamine and picoline or a mixture of several of them. Others are the same as in the seventh embodiment.

具体实施方式九:本实施方式与具体实施方式七或八之一不同的是:步骤一中所述的高沸点叔胺为三正丁胺、三异丙醇胺和二甲胺基甲酰氯中的一种或其中几种的混合物。其它与具体实施方式七或八相同。Specific embodiment nine: the difference between this embodiment and one of specific embodiment seven or eight is: the high boiling point tertiary amine described in step one is tri-n-butylamine, triisopropanolamine and dimethylcarbamoyl chloride one or a mixture of several of them. Others are the same as the seventh or eighth specific embodiment.

具体实施方式十:本实施方式与具体实施方式七至九之一不同的是:步骤一中所述的水性脱模剂为在温度小于100℃的条件下能与水互溶,且不析出的脱模剂或离型剂。其它与具体实施方式七至九相同。Embodiment 10: The difference between this embodiment and one of Embodiments 7 to 9 is that the water-based release agent described in step 1 is a release agent that is miscible with water and does not precipitate when the temperature is less than 100°C. Molding agent or release agent. Others are the same as the seventh to ninth embodiments.

具体实施方式十一:本实施方式与具体实施方式七至十之一不同的是:步骤一中所述的水性脱模剂为RPLUS S02-004、Sepaluck RA715W、Sepaluck RA733W、NS-100或Sepaluck RA780W。其它与具体实施方式七至十相同。Embodiment 11: The difference between this embodiment and embodiment 7 to 11 is that the water-based release agent described in step 1 is RPLUS S02-004, Sepaluck RA715W, Sepaluck RA733W, NS-100 or Sepaluck RA780W . Others are the same as Embodiments 7 to 10.

RPLUS S02-004为德国克鲁勃公司生产;Sepaluck RA715W、Sepaluck RA733W、NS-100和Sepaluck RA780W为日本山一化学公司生产。RPLUS S02-004 is produced by Klüber Company in Germany; Sepaluck RA715W, Sepaluck RA733W, NS-100 and Sepaluck RA780W are produced by Yamaichi Chemical Company in Japan.

具体实施方式十二:本实施方式与具体实施方式七至十一之一不同的是:步骤一中所述的芳香二酐和芳香二胺的总质量与极性溶剂的质量比为1:(0~1.5);步骤一中所述的低沸点叔胺与高沸点叔胺的摩尔比例为1:(0.5~100)。其它与具体实施方式七至十一相同。Embodiment 12: The difference between this embodiment and Embodiment 7 to 11 is that the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine described in step 1 to the polar solvent is 1:( 0~1.5); The molar ratio of the low boiling point tertiary amine and the high boiling point tertiary amine described in step one is 1:(0.5~100). Others are the same as Embodiments 7 to 11.

本具体实施方式芳香二酐和芳香二胺的总质量与极性溶剂的质量比能提供低溶剂负担且保持较好效果。In this specific embodiment, the mass ratio of the total mass of aromatic dianhydride and aromatic diamine to the polar solvent can provide low solvent burden and maintain a good effect.

具体实施方式十三:本实施方式的利用一种聚酰亚胺前驱体溶液制备聚酰亚胺薄膜的方法,具体是按以下步骤进行的:Specific Embodiment Thirteen: The method for preparing a polyimide film using a polyimide precursor solution in this embodiment is specifically carried out in the following steps:

一、将聚酰亚胺前驱体溶液过滤并脱气,沿着T型狭缝流延到不锈钢制转鼓上,然后在温度为60℃~180℃下,干燥1min~50min,得到自支撑薄膜;1. Filter and degas the polyimide precursor solution, cast it on a stainless steel drum along the T-shaped slit, and then dry it at a temperature of 60 ° C to 180 ° C for 1 min to 50 min to obtain a self-supporting film ;

二、将自支撑薄膜从不锈钢制转鼓上剥离并置于固化炉中固化,首先在温度为150℃~200℃的条件下,加热1min~60min,再在温度为200℃~250℃的条件下,加热1min~60min,然后在温度为250℃~450℃的条件下,加热1min~60min,最后在温度为290℃~310℃的条件下,退火处理约1min~20min,得到聚酰亚胺薄膜;2. Peel the self-supporting film from the stainless steel drum and place it in a curing furnace for curing. First, heat it for 1min to 60min at a temperature of 150°C to 200°C, and then heat it at a temperature of 200°C to 250°C. , heating for 1min to 60min, then heating for 1min to 60min at a temperature of 250°C to 450°C, and finally annealing for about 1min to 20min at a temperature of 290°C to 310°C to obtain polyimide film;

且固化过程中利用夹具夹持自支撑薄膜,使得自支撑薄膜固化前后纵向长度变化百分率为5%~20%,横向长度变化百分率为10%~80%。And during the curing process, the self-supporting film is clamped by a clamp, so that the percentage change of the longitudinal length of the self-supporting film before and after curing is 5%-20%, and the percentage change of the transverse length is 10%-80%.

本实施方式的聚酰亚胺薄膜可以通过使作为前驱体的聚酰胺酸酰亚胺化得到。此外,在其制造中可以使用工人的原料、反应条件等。此外,可以根据功能需要添加无机或有机物的填料。The polyimide film of this embodiment can be obtained by imidating the polyamic acid which is a precursor. In addition, workers' raw materials, reaction conditions, etc. may be used in its manufacture. In addition, inorganic or organic fillers can be added according to functional needs.

接着将自支撑膜从基板表面剥离进行固化工序,可以通过浸渍水溶液、给与额外张力等方法实现。Next, the self-supporting film is peeled off from the surface of the substrate to carry out the curing process, which can be achieved by immersing in an aqueous solution, applying additional tension, and the like.

聚酰亚胺薄膜是根据聚酰亚胺前驱体溶液获得的聚酰亚胺薄膜。作为聚酰亚胺薄膜可以作为液晶取向膜、燃料电池用多孔聚酰亚胺薄膜、分离膜、PCB板单层、双层、多层、R-F、HDI用薄膜基板、电线电缆用绝缘膜、耐高温薄膜等。The polyimide film is a polyimide film obtained from a polyimide precursor solution. As a polyimide film, it can be used as liquid crystal alignment film, porous polyimide film for fuel cells, separation membrane, PCB board single layer, double layer, multilayer, R-F, HDI film substrate, insulating film for wire and cable, High temperature film etc.

本实施方式的有益效果是:本实施方式提供的一种聚酰亚胺前驱体溶液及其制备方法和利用其制备聚酰亚胺薄膜的方法,可以解决现有聚酰亚胺前驱体-聚酰胺酸水溶液的制备方法和结构组成难以实现在流延设备生产高表面质量和连续化不脆裂的聚酰亚胺薄膜的问题。根据聚酰亚胺前驱体溶液的制备方法,采用了低比例高沸点极性溶剂、多种沸点叔胺复合物的组合。The beneficial effect of this embodiment is: a kind of polyimide precursor solution provided by this embodiment and its preparation method and the method for using it to prepare polyimide film can solve the problem of existing polyimide precursor - polyimide The preparation method and structural composition of the amic acid aqueous solution are difficult to realize the problem of producing high surface quality and continuous non-brittle polyimide films in tape casting equipment. According to the preparation method of the polyimide precursor solution, a combination of a low-proportion high-boiling-point polar solvent and various boiling-point tertiary amine compounds is used.

一方面,利用高沸点极性溶剂(如N,N-二甲基乙酰胺、N,N-二甲基甲酰胺等)与水的组合,提高溶剂整体沸点,避免形成的自支撑聚酰亚胺前驱体薄膜含溶剂量过少(少于20%)和沸点低,虽然自支撑膜依然经历高温亚胺化(有拉伸作用或无拉伸作用)过程(150℃-250℃)中会出现分子量下降和强度下降的情况,但是含溶剂量的提升和沸点提高,极大程度提高了初始亚胺化(150℃-200℃)的伸长率和柔韧性,避免了在高温由于外部载荷导致的薄膜断裂的危险,影响薄膜连续化操作。On the one hand, use the combination of high boiling point polar solvents (such as N,N-dimethylacetamide, N,N-dimethylformamide, etc.) and water to increase the overall boiling point of the solvent and avoid the formation of self-supporting polyimide The amine precursor film contains too little solvent (less than 20%) and has a low boiling point. Although the self-supporting film still undergoes high-temperature imidization (with or without stretching) process (150°C-250°C), it will There is a decrease in molecular weight and a decrease in strength, but the increase in solvent content and the increase in boiling point greatly improve the elongation and flexibility of the initial imidization (150°C-200°C), avoiding the high temperature due to external load The resulting danger of film breakage affects the continuous operation of the film.

另一方面,聚酰亚胺前驱体溶液制备方法采用了多种沸点叔胺复合物,从而在流延脱出溶剂形成自支撑膜时,仍含有多种沸点叔胺在前驱体中。在亚胺化程序中将自支撑膜倒入固化炉进行处理,尤其是对于连续化的处理自支撑膜的热亚胺化,需要施加一定的轴向外部载荷提供牵引,在水分基本挥发后(<150℃),常用单一叔胺类也面临在150℃下挥发的风险,难以作为液态残留提升弥补初始亚胺化后(150℃-250℃)低强度、低伸长率。采用多种叔胺提供多种脱除温度和沸点,实现在大于150℃时仍保留有一定液态残留。并且和高沸点溶剂组合的方式复合使用,能够进一步确保在亚胺化初始温度条件下的薄膜持续伸长和膨胀系数,极大避免了在亚胺化初始的薄膜破坏,尤其是受到牵引力作用下薄膜的破坏,从而节省了固化炉降温、重新穿膜、升温的电力和时间成本。On the other hand, the polyimide precursor solution preparation method uses a variety of boiling point tertiary amine complexes, so that when the solvent is cast out to form a self-supporting film, the precursor still contains a variety of boiling point tertiary amines. In the imidization process, the self-supporting film is poured into the curing furnace for processing, especially for the thermal imidization of the self-supporting film for continuous treatment, it is necessary to apply a certain axial external load to provide traction. After the water is basically volatilized ( <150°C), commonly used single tertiary amines also face the risk of volatilization at 150°C, and it is difficult to improve the low strength and low elongation after initial imidization (150°C-250°C) as a liquid residue. A variety of tertiary amines are used to provide a variety of removal temperatures and boiling points to achieve a certain liquid residue at temperatures above 150°C. And combined with high boiling point solvents, it can further ensure the continuous elongation and expansion coefficient of the film at the initial temperature of imidization, and greatly avoid the film damage at the initial imidization, especially under the action of traction The destruction of the film saves the cost of electricity and time for cooling the curing furnace, re-piercing the film, and heating up.

出乎意料的是,多种叔胺的复合使用,不仅有利于提升薄膜各阶段成型强度,同时还提高了薄膜的表面质量和降低了缺陷。由于低沸点的单一叔胺和水在挥发后,聚酰亚胺前驱体面临快速亚胺化和溶剂、催化剂脱出的双重压力,会严重导致的薄膜表面平整度差、表面有挥发脱出留下的气孔、亚胺化短时脱除大量水留下的闭孔等,对薄膜的表面质量有很大影响。采用低沸点和高沸点叔胺并用的方式,出乎意料的获得了不同亚胺化条件下持续的挥发效果,使聚酰亚胺薄膜形成过程中不依靠外力而提供自流平的效果,极大的解决了薄膜的表面质量问题。尤其是对于连续化薄膜的热亚胺化操作,不仅减少了褶皱和空隙的出现,薄膜平整度也得到增强。且具体实施方式制备的聚酰亚胺前驱体溶液还可用于形成聚酰亚胺纤维。Unexpectedly, the combined use of various tertiary amines not only helps to improve the forming strength of the film at each stage, but also improves the surface quality of the film and reduces defects. After the single tertiary amine with a low boiling point and water volatilize, the polyimide precursor faces the double pressure of rapid imidization and solvent and catalyst detachment, which will seriously cause poor surface roughness of the film and surface left by volatilization. Pores, closed pores left by removing a large amount of water in a short period of imidization, etc., have a great influence on the surface quality of the film. Using the combination of low-boiling point and high-boiling point tertiary amines, unexpectedly obtained the continuous volatilization effect under different imidization conditions, so that the polyimide film formation process does not rely on external forces to provide self-leveling effect, greatly It solves the surface quality problem of the film. Especially for the thermal imidization operation of continuous film, not only the occurrence of wrinkles and voids is reduced, but also the flatness of the film is enhanced. And the polyimide precursor solution prepared in the specific embodiment can also be used to form polyimide fibers.

具体实施方式十四:本实施方式与具体实施方式十三不同的是:步骤一中然后在温度为80℃~160℃下,干燥10min~30min。其它与具体实施方式十三相同。Embodiment 14: This embodiment is different from Embodiment 13 in that: in step 1, dry at a temperature of 80° C. to 160° C. for 10 minutes to 30 minutes. Others are the same as in the thirteenth embodiment.

本实施方式的有益效果是:The beneficial effects of this embodiment are:

采用以下实施例验证本发明的有益效果:Adopt the following examples to verify the beneficial effects of the present invention:

实施例一:Embodiment one:

一种聚酰亚胺前驱体溶液由叔胺、水性脱模剂、芳香二酐、芳香二胺、极性溶剂及水制成;A polyimide precursor solution is made of tertiary amine, aqueous release agent, aromatic dianhydride, aromatic diamine, polar solvent and water;

所述的芳香二胺与叔胺的摩尔比为1:0.05;所述的芳香二胺与水性脱模剂的质量比为1:0.01;所述的芳香二胺与芳香二酐的摩尔比为1:1;所述的芳香二酐和芳香二胺的总质量与水的质量比为1:8;所述的芳香二酐和芳香二胺的总质量与极性溶剂的质量比为1:1;The molar ratio of the aromatic diamine to the tertiary amine is 1:0.05; the mass ratio of the aromatic diamine to the aqueous release agent is 1:0.01; the molar ratio of the aromatic diamine to the aromatic dianhydride is 1:1; the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to water is 1:8; the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to the polar solvent is 1: 1;

所述的芳香二胺为对苯二胺;Described aromatic diamine is p-phenylenediamine;

所述的叔胺为二乙醇单异丙醇胺;Described tertiary amine is diethanol monoisopropanolamine;

所述的极性溶剂为N,N-二甲基乙酰胺;所述的水性脱模剂为日本山一化学公司生产的NS-100;The polar solvent is N,N-dimethylacetamide; the water-based release agent is NS-100 produced by Japan Yamaichi Chemical Company;

所述的芳香二酐为3,3,4′,4′-联苯四羧酸二酐,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:The aromatic dianhydride is 3,3,4′,4′-biphenyltetracarboxylic dianhydride, and the repeating unit of polyamic acid in the polyimide precursor solution is:

上述一种聚酰亚胺前驱体溶液的制备方法是按以下步骤进行:The preparation method of above-mentioned a kind of polyimide precursor solution is to carry out as follows:

一、取8.16g二乙醇单异丙醇胺(0.05mol)、1.08g NS-100、294.22g 3,3,4’,4’-联苯四羧酸二酐(1mol)、108.14g对苯二胺(1mol)、402.36g N,N-二甲基乙酰胺及3218.88g水;1. Take 8.16g diethanol monoisopropanolamine (0.05mol), 1.08g NS-100, 294.22g 3,3,4',4'-biphenyltetracarboxylic dianhydride (1mol), 108.14g p-phenylene Diamine (1mol), 402.36g N,N-dimethylacetamide and 3218.88g water;

二、在氮气气氛、温度为5℃及搅拌条件下,向三颈瓶中加入3218.88g水和402.36gN,N-二甲基乙酰胺,然后加入108.14g对苯二胺(1mol),得到反应液,将294.22g 3,3,4’,4’-联苯四羧酸二酐(1mol)按质量平均分三次加入到反应液中,反应5h,然后将反应液升温至20℃,在氮气气氛、温度为20℃及搅拌条件下,向反应液中加入8.16g二乙醇单异丙醇胺(0.05mol)和1.08g NS-100,搅拌反应5h,最后将反应液温度降低至5℃,静置10h,得到聚酰亚胺前驱体溶液;2. In a nitrogen atmosphere, at a temperature of 5°C and under stirring conditions, add 3218.88g of water and 402.36g of N,N-dimethylacetamide to a three-necked flask, and then add 108.14g of p-phenylenediamine (1mol) to obtain a reaction Liquid, 294.22g 3,3,4',4'-biphenyltetracarboxylic dianhydride (1mol) was added to the reaction liquid in three times according to the mass average, and reacted for 5h, then the reaction liquid was heated to 20 ° C, under nitrogen Under the condition of atmosphere and temperature of 20°C and stirring, add 8.16g of diethanol monoisopropanolamine (0.05mol) and 1.08g of NS-100 to the reaction solution, stir for 5 hours, and finally lower the temperature of the reaction solution to 5°C. Leave standstill 10h, obtain polyimide precursor solution;

利用上述一种聚酰亚胺前驱体溶液制备聚酰亚胺薄膜的方法是按以下步骤进行:The method that utilizes above-mentioned a kind of polyimide precursor solution to prepare polyimide film is to carry out as follows:

一、将聚酰亚胺前驱体溶液过滤并脱气,沿着T型狭缝流延到不锈钢制转鼓上,然后在温度为120℃下,干燥10min,得到自支撑薄膜;1. Filter and degas the polyimide precursor solution, cast it onto a stainless steel drum along the T-shaped slit, and then dry it at 120°C for 10 minutes to obtain a self-supporting film;

二、将自支撑薄膜从不锈钢制转鼓上剥离并置于固化炉中固化,首先在温度为150℃的条件下,加热3min,再在温度为250℃的条件下,加热3min,然后在温度为400℃的条件下,加热70s,最后在温度为300℃的条件下,退火处理约1min,得到聚酰亚胺薄膜;2. Peel the self-supporting film from the stainless steel drum and place it in a curing furnace for curing. First, heat it for 3 minutes at a temperature of 150°C, then heat it for 3 minutes at a temperature of 250°C, and then heat it at a temperature of 250°C. Heating at 400°C for 70s, and finally annealing at 300°C for about 1 min to obtain a polyimide film;

且固化过程中利用夹具夹持自支撑薄膜,使得自支撑薄膜固化前后纵向长度变化百分率为10%,横向长度变化百分率为50%。And during the curing process, the self-supporting film is clamped by a clamp, so that the percentage change of the longitudinal length of the self-supporting film before and after curing is 10%, and the percentage change of the transverse length is 50%.

本实施例制备的聚酰亚胺薄膜的厚度为25微米。The thickness of the polyimide film prepared in this embodiment is 25 microns.

实施例二:Embodiment two:

一种聚酰亚胺前驱体溶液由叔胺、水性脱模剂、芳香二酐、芳香二胺、极性溶剂及水制成;A polyimide precursor solution is made of tertiary amine, aqueous release agent, aromatic dianhydride, aromatic diamine, polar solvent and water;

所述的芳香二胺与叔胺的摩尔比为1:0.05;所述的芳香二胺与水性脱模剂的质量比为1:0.01;所述的芳香二胺与芳香二酐的摩尔比为1:1;所述的芳香二酐和芳香二胺的总质量与水的质量比为1:8;所述的芳香二酐和芳香二胺的总质量与极性溶剂的质量比为1:1;The molar ratio of the aromatic diamine to the tertiary amine is 1:0.05; the mass ratio of the aromatic diamine to the aqueous release agent is 1:0.01; the molar ratio of the aromatic diamine to the aromatic dianhydride is 1:1; the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to water is 1:8; the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to the polar solvent is 1: 1;

所述的芳香二胺为4,4′-二氨基二苯醚;The aromatic diamine is 4,4'-diaminodiphenyl ether;

所述的叔胺为二乙醇单异丙醇胺;Described tertiary amine is diethanol monoisopropanolamine;

所述的极性溶剂为N,N-二甲基乙酰胺;The polar solvent is N,N-dimethylacetamide;

所述的水性脱模剂为日本山一化学公司生产的NS-100;The water-based release agent is NS-100 produced by Japan Yamaichi Chemical Company;

所述的芳香二酐为均苯四甲酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride is pyromellitic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is:

上述一种聚酰亚胺前驱体溶液的制备方法是按以下步骤进行:The preparation method of above-mentioned a kind of polyimide precursor solution is to carry out as follows:

一、取8.16g的二乙醇单异丙醇胺(0.05mol)、2.00g的NS-100、218.12g的均苯四甲酸二酐(1mol)、200.24g的4,4’-二氨基二苯醚(1mol)、418.36g的N,N-二甲基乙酰胺及3346.88g的水;1. Take 8.16g of diethanol monoisopropanolamine (0.05mol), 2.00g of NS-100, 218.12g of pyromellitic dianhydride (1mol), 200.24g of 4,4'-diaminodiphenyl Ether (1mol), 418.36g of N,N-dimethylacetamide and 3346.88g of water;

二、在氮气气氛、温度为5℃及搅拌条件下,向三颈瓶中加入称取的3346.88g的水和418.36g的N,N-二甲基乙酰胺,然后加入200.24g的4,4’-二氨基二苯醚(1mol),得到反应液,将218.12g的均苯四甲酸二酐(1mol)按质量平均分三次加入到反应液中,反应2h,然后将反应液升温至20℃,在氮气气氛、温度为20℃及搅拌条件下,向反应液中加入8.16g的二乙醇单异丙醇胺(0.05mol)和2.00g的NS-100,搅拌反应5h,最后将反应液温度降低至5℃,静置10h,得到聚酰亚胺前驱体溶液;2. In a nitrogen atmosphere, at a temperature of 5°C and under stirring conditions, add 3346.88 g of water and 418.36 g of N,N-dimethylacetamide into the three-necked flask, and then add 200.24 g of 4,4 '-Diaminodiphenyl ether (1mol) to obtain a reaction solution, 218.12g of pyromellitic dianhydride (1mol) was added to the reaction solution in three equal parts by mass, reacted for 2h, and then the reaction solution was heated to 20°C , under a nitrogen atmosphere, a temperature of 20°C and stirring conditions, add 8.16g of diethanol monoisopropanolamine (0.05mol) and 2.00g of NS-100 to the reaction solution, stir the reaction for 5h, and finally reduce the temperature of the reaction solution to Decrease to 5°C and let it stand for 10 hours to obtain a polyimide precursor solution;

利用上述一种聚酰亚胺前驱体溶液制备聚酰亚胺薄膜的方法是按以下步骤进行:The method that utilizes above-mentioned a kind of polyimide precursor solution to prepare polyimide film is to carry out as follows:

一、将聚酰亚胺前驱体溶液过滤并脱气,沿着T型狭缝流延到不锈钢制转鼓上,然后在温度为120℃下,干燥10min,得到自支撑薄膜;1. Filter and degas the polyimide precursor solution, cast it onto a stainless steel drum along the T-shaped slit, and then dry it at 120°C for 10 minutes to obtain a self-supporting film;

二、将自支撑薄膜从不锈钢制转鼓上剥离并置于固化炉中固化,首先在温度为150℃的条件下,加热3min,再在温度为250℃的条件下,加热3min,然后在温度为400℃的条件下,加热70s,最后在温度为300℃的条件下,退火处理约1min,得到聚酰亚胺薄膜;2. Peel the self-supporting film from the stainless steel drum and place it in a curing furnace for curing. First, heat it for 3 minutes at a temperature of 150°C, then heat it for 3 minutes at a temperature of 250°C, and then heat it at a temperature of 250°C. Heating at 400°C for 70s, and finally annealing at 300°C for about 1 min to obtain a polyimide film;

且固化过程中利用夹具夹持自支撑薄膜,使得自支撑薄膜固化前后纵向长度变化百分率为10%,横向长度变化百分率为50%。And during the curing process, the self-supporting film is clamped by a clamp, so that the percentage change of the longitudinal length of the self-supporting film before and after curing is 10%, and the percentage change of the transverse length is 50%.

本实施例制备的聚酰亚胺薄膜的厚度为25微米。The thickness of the polyimide film prepared in this embodiment is 25 microns.

实施例三:Embodiment three:

一种聚酰亚胺前驱体溶液由叔胺、水性脱模剂、芳香二酐、芳香二胺及水制成;A polyimide precursor solution is made of tertiary amine, aqueous release agent, aromatic dianhydride, aromatic diamine and water;

所述的芳香二胺与叔胺的摩尔比为1:0.05;所述的芳香二胺与水性脱模剂的质量比为1:0.01;所述的芳香二胺与芳香二酐的摩尔比为1:1;所述的芳香二酐和芳香二胺的总质量与水的质量比为1:9;The molar ratio of the aromatic diamine to the tertiary amine is 1:0.05; the mass ratio of the aromatic diamine to the aqueous release agent is 1:0.01; the molar ratio of the aromatic diamine to the aromatic dianhydride is 1:1; the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to water is 1:9;

所述的芳香二胺为对苯二胺;Described aromatic diamine is p-phenylenediamine;

所述的叔胺为低沸点叔胺与高沸点叔胺的混合物,所述的低沸点叔胺与高沸点叔胺的摩尔比例为1:1;The tertiary amine is a mixture of a low-boiling tertiary amine and a high-boiling tertiary amine, and the molar ratio of the low-boiling tertiary amine to the high-boiling tertiary amine is 1:1;

所述的低沸点叔胺为二乙醇单异丙醇胺;Described low boiling point tertiary amine is diethanol monoisopropanolamine;

所述的高沸点叔胺为二甲胺基甲酰氯;Described high boiling point tertiary amine is dimethylcarbamoyl chloride;

所述的水性脱模剂为日本山一化学公司生产的NS-100;The water-based release agent is NS-100 produced by Japan Yamaichi Chemical Company;

所述的芳香二酐为3,3,4′,4′-联苯四羧酸二酐,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:The aromatic dianhydride is 3,3,4′,4′-biphenyltetracarboxylic dianhydride, and the repeating unit of polyamic acid in the polyimide precursor solution is:

上述一种聚酰亚胺前驱体溶液的制备方法是按以下步骤进行:The preparation method of above-mentioned a kind of polyimide precursor solution is to carry out as follows:

一、取4.08g的二乙醇单异丙醇胺(0.025mol)、2.69g的二甲胺基甲酰氯(0.025mol)、1.08g的NS-100、294.22g的3,3,4’,4’-联苯四羧酸二酐(1mol)、108.14g的对苯二胺(1mol)及3621.24g的水;1. Take 4.08g of diethanol monoisopropanolamine (0.025mol), 2.69g of dimethylcarbamoyl chloride (0.025mol), 1.08g of NS-100, 294.22g of 3,3,4',4 '-biphenyltetracarboxylic dianhydride (1mol), 108.14g of p-phenylenediamine (1mol) and 3621.24g of water;

二、在氮气气氛、温度为5℃及搅拌条件下,向三颈瓶中加入3621.24g的水,然后加入108.14g的对苯二胺(1mol),得到反应液,将294.22g的3,3,4’,4’-联苯四羧酸二酐(1mol)按质量平均分三次加入到反应液中,反应5h,然后将反应液升温至20℃,在氮气气氛、温度为20℃及搅拌条件下,向反应液中加入4.08g的二乙醇单异丙醇胺(0.025mol)、2.69g的二甲胺基甲酰氯(0.025mol)和1.08g的NS-100,搅拌反应5h,最后将反应液温度降低至5℃,静置10h,得到聚酰亚胺前驱体溶液;2. In a nitrogen atmosphere, at a temperature of 5°C and under stirring conditions, add 3621.24g of water to the three-necked flask, then add 108.14g of p-phenylenediamine (1mol) to obtain a reaction solution, and 294.22g of 3,3 , 4',4'-biphenyltetracarboxylic dianhydride (1mol) was added to the reaction liquid in three times according to the mass average, reacted for 5h, and then the reaction liquid was heated to 20°C, in a nitrogen atmosphere, the temperature was 20°C and stirred Under conditions, add 4.08g of diethanol monoisopropanolamine (0.025mol), 2.69g of dimethylcarbamoyl chloride (0.025mol) and 1.08g of NS-100 to the reaction solution, stir the reaction for 5h, and finally The temperature of the reaction solution was lowered to 5° C., and allowed to stand for 10 hours to obtain a polyimide precursor solution;

利用上述一种聚酰亚胺前驱体溶液制备聚酰亚胺薄膜的方法是按以下步骤进行:The method that utilizes above-mentioned a kind of polyimide precursor solution to prepare polyimide film is to carry out as follows:

一、将聚酰亚胺前驱体溶液过滤并脱气,沿着T型狭缝流延到不锈钢制转鼓上,然后在温度为120℃下,干燥10min,得到自支撑薄膜;1. Filter and degas the polyimide precursor solution, cast it onto a stainless steel drum along the T-shaped slit, and then dry it at 120°C for 10 minutes to obtain a self-supporting film;

二、将自支撑薄膜从不锈钢制转鼓上剥离并置于固化炉中固化,首先在温度为150℃的条件下,加热3min,再在温度为250℃的条件下,加热3min,然后在温度为400℃的条件下,加热70s,最后在温度为300℃的条件下,退火处理约1min,得到聚酰亚胺薄膜;2. Peel the self-supporting film from the stainless steel drum and place it in a curing furnace for curing. First, heat it for 3 minutes at a temperature of 150°C, then heat it for 3 minutes at a temperature of 250°C, and then heat it at a temperature of 250°C. Heating at 400°C for 70s, and finally annealing at 300°C for about 1 min to obtain a polyimide film;

且固化过程中利用夹具夹持自支撑薄膜,使得自支撑薄膜固化前后纵向长度变化百分率为10%,横向长度变化百分率为50%。And during the curing process, the self-supporting film is clamped by a clamp, so that the percentage change of the longitudinal length of the self-supporting film before and after curing is 10%, and the percentage change of the transverse length is 50%.

本实施例制备的聚酰亚胺薄膜的厚度为25微米。The thickness of the polyimide film prepared in this embodiment is 25 microns.

实施例四:Embodiment four:

一种聚酰亚胺前驱体溶液由叔胺、水性脱模剂、芳香二酐、芳香二胺、极性溶剂及水制成;A polyimide precursor solution is made of tertiary amine, aqueous release agent, aromatic dianhydride, aromatic diamine, polar solvent and water;

所述的芳香二胺与叔胺的摩尔比为1:0.05;所述的芳香二胺与水性脱模剂的质量比为1:0.01;所述的芳香二胺与芳香二酐的摩尔比为1:1;所述的芳香二酐和芳香二胺的总质量与水的质量比为1:8;所述的芳香二酐和芳香二胺的总质量与极性溶剂的质量比为1:1;The molar ratio of the aromatic diamine to the tertiary amine is 1:0.05; the mass ratio of the aromatic diamine to the aqueous release agent is 1:0.01; the molar ratio of the aromatic diamine to the aromatic dianhydride is 1:1; the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to water is 1:8; the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to the polar solvent is 1: 1;

所述的芳香二胺为对苯二胺;Described aromatic diamine is p-phenylenediamine;

所述的叔胺为低沸点叔胺与高沸点叔胺的混合物,所述的低沸点叔胺与高沸点叔胺的摩尔比例为1:1;The tertiary amine is a mixture of a low-boiling tertiary amine and a high-boiling tertiary amine, and the molar ratio of the low-boiling tertiary amine to the high-boiling tertiary amine is 1:1;

所述的低沸点叔胺为二乙醇单异丙醇胺;Described low boiling point tertiary amine is diethanol monoisopropanolamine;

所述的高沸点叔胺为二甲胺基甲酰氯;Described high boiling point tertiary amine is dimethylcarbamoyl chloride;

所述的极性溶剂为N,N-二甲基乙酰胺;The polar solvent is N,N-dimethylacetamide;

所述的水性脱模剂为日本山一化学公司生产的NS-100;The water-based release agent is NS-100 produced by Japan Yamaichi Chemical Company;

所述的芳香二酐为3,3,4′,4′-联苯四羧酸二酐,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:The aromatic dianhydride is 3,3,4′,4′-biphenyltetracarboxylic dianhydride, and the repeating unit of polyamic acid in the polyimide precursor solution is:

上述一种聚酰亚胺前驱体溶液的制备方法是按以下步骤进行:The preparation method of above-mentioned a kind of polyimide precursor solution is to carry out as follows:

一、取4.08g的二乙醇单异丙醇胺(0.025mol)、2.69g的二甲胺基甲酰氯(0.025mol)、1.08g的NS-100、294.22g的3,3,4’,4’-联苯四羧酸二酐(1mol)、108.14g的对苯二胺(1mol)、402.36g的N,N-二甲基乙酰胺及3218.88g的水;1. Take 4.08g of diethanol monoisopropanolamine (0.025mol), 2.69g of dimethylcarbamoyl chloride (0.025mol), 1.08g of NS-100, 294.22g of 3,3,4',4 '-biphenyltetracarboxylic dianhydride (1mol), 108.14g of p-phenylenediamine (1mol), 402.36g of N,N-dimethylacetamide and 3218.88g of water;

二、在氮气气氛、温度为5℃及搅拌条件下,向三颈瓶中加入3218.88g的水和402.36g的N,N-二甲基乙酰胺,然后加入108.14g的对苯二胺(1mol),得到反应液,将294.22g的3,3,4’,4’-联苯四羧酸二酐(1mol)按质量平均分三次加入到反应液中,反应5h,然后将反应液升温至20℃,在氮气气氛、温度为20℃及搅拌条件下,向反应液中加入4.08g的二乙醇单异丙醇胺(0.025mol)、2.69g的二甲胺基甲酰氯(0.025mol)和1.08g的NS-100,搅拌反应5h,最后将反应液温度降低至5℃,静置10h,得到聚酰亚胺前驱体溶液;2. In a nitrogen atmosphere, at a temperature of 5°C and under stirring conditions, add 3218.88g of water and 402.36g of N,N-dimethylacetamide into the three-necked flask, and then add 108.14g of p-phenylenediamine (1mol ), to obtain the reaction solution, 294.22g of 3,3,4',4'-biphenyltetracarboxylic dianhydride (1mol) was added to the reaction solution in three times by mass average, reacted for 5h, and then the reaction solution was heated to 20 DEG C, under nitrogen atmosphere, temperature is 20 DEG C and under stirring condition, add the diethanol monoisopropanolamine (0.025mol) of 4.08g, the dimethylcarbamoyl chloride (0.025mol) of 2.69g and 1.08g of NS-100, stirred and reacted for 5h, and finally lowered the temperature of the reaction solution to 5°C, and stood still for 10h to obtain a polyimide precursor solution;

利用上述一种聚酰亚胺前驱体溶液制备聚酰亚胺薄膜的方法是按以下步骤进行:The method that utilizes above-mentioned a kind of polyimide precursor solution to prepare polyimide film is to carry out as follows:

一、将聚酰亚胺前驱体溶液过滤并脱气,沿着T型狭缝流延到不锈钢制转鼓上,然后在温度为120℃下,干燥10min,得到自支撑薄膜;1. Filter and degas the polyimide precursor solution, cast it onto a stainless steel drum along the T-shaped slit, and then dry it at 120°C for 10 minutes to obtain a self-supporting film;

二、将自支撑薄膜从不锈钢制转鼓上剥离并置于固化炉中固化,首先在温度为150℃的条件下,加热3min,再在温度为250℃的条件下,加热3min,然后在温度为400℃的条件下,加热70s,最后在温度为300℃的条件下,退火处理约1min,得到聚酰亚胺薄膜;2. Peel the self-supporting film from the stainless steel drum and place it in a curing furnace for curing. First, heat it for 3 minutes at a temperature of 150°C, then heat it for 3 minutes at a temperature of 250°C, and then heat it at a temperature of 250°C. Heating at 400°C for 70s, and finally annealing at 300°C for about 1 min to obtain a polyimide film;

且固化过程中利用夹具夹持自支撑薄膜,使得自支撑薄膜固化前后纵向长度变化百分率为10%,横向长度变化百分率为50%。And during the curing process, the self-supporting film is clamped by a clamp, so that the percentage change of the longitudinal length of the self-supporting film before and after curing is 10%, and the percentage change of the transverse length is 50%.

本实施例制备的聚酰亚胺薄膜的厚度为25微米。The thickness of the polyimide film prepared in this embodiment is 25 microns.

实施例五:Embodiment five:

一种聚酰亚胺前驱体溶液由叔胺、水性脱模剂、芳香二酐、芳香二胺、极性溶剂及水制成;A polyimide precursor solution is made of tertiary amine, aqueous release agent, aromatic dianhydride, aromatic diamine, polar solvent and water;

所述的芳香二胺与叔胺的摩尔比为1:0.05;所述的芳香二胺与水性脱模剂的质量比为1:0.01;所述的芳香二胺与芳香二酐的摩尔比为1:1;所述的芳香二酐和芳香二胺的总质量与水的质量比为1:8;所述的芳香二酐和芳香二胺的总质量与极性溶剂的质量比为1:1;The molar ratio of the aromatic diamine to the tertiary amine is 1:0.05; the mass ratio of the aromatic diamine to the aqueous release agent is 1:0.01; the molar ratio of the aromatic diamine to the aromatic dianhydride is 1:1; the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to water is 1:8; the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to the polar solvent is 1: 1;

所述的芳香二胺为对苯二胺;Described aromatic diamine is p-phenylenediamine;

所述的叔胺为低沸点叔胺与高沸点叔胺的混合物,所述的低沸点叔胺与高沸点叔胺的摩尔比例为1:1;The tertiary amine is a mixture of a low-boiling tertiary amine and a high-boiling tertiary amine, and the molar ratio of the low-boiling tertiary amine to the high-boiling tertiary amine is 1:1;

所述的低沸点叔胺为二乙醇单异丙醇胺;Described low boiling point tertiary amine is diethanol monoisopropanolamine;

所述的高沸点叔胺为二甲胺基甲酰氯;Described high boiling point tertiary amine is dimethylcarbamoyl chloride;

所述的极性溶剂为N,N-二甲基乙酰胺;The polar solvent is N,N-dimethylacetamide;

所述的水性脱模剂为日本山一化学公司生产的NS-100;The water-based release agent is NS-100 produced by Japan Yamaichi Chemical Company;

所述的芳香二酐为3,3,4′,4′-联苯四羧酸二酐,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:The aromatic dianhydride is 3,3,4′,4′-biphenyltetracarboxylic dianhydride, and the repeating unit of polyamic acid in the polyimide precursor solution is:

上述一种聚酰亚胺前驱体溶液的制备方法是按以下步骤进行:The preparation method of above-mentioned a kind of polyimide precursor solution is to carry out as follows:

一、取4.08g的二乙醇单异丙醇胺(0.025mol)、2.69g的二甲胺基甲酰氯(0.025mol)和1.08g的NS-100、294.22g的3,3,4’,4’-联苯四羧酸二酐(1mol)、108.14g的对苯二胺(1mol)、402.36g的N,N-二甲基乙酰胺及3218.88g的水;1. Take 4.08g of diethanol monoisopropanolamine (0.025mol), 2.69g of dimethylcarbamoyl chloride (0.025mol) and 1.08g of NS-100, 294.22g of 3,3,4',4 '-biphenyltetracarboxylic dianhydride (1mol), 108.14g of p-phenylenediamine (1mol), 402.36g of N,N-dimethylacetamide and 3218.88g of water;

二、在氮气气氛、温度为5℃及搅拌条件下,向三颈瓶中加入3218.88g的水和402.36g的N,N-二甲基乙酰胺,然后加入108.14g的对苯二胺(1mol),得到反应液,将294.22g的3,3,4’,4’-联苯四羧酸二酐(1mol)按质量平均分三次加入到反应液中,反应5h,然后将反应液升温至20℃,在氮气气氛、温度为20℃及搅拌条件下,向反应液中加入4.08g的二乙醇单异丙醇胺(0.025mol)、2.69g的二甲胺基甲酰氯(0.025mol)和1.08g的NS-100,搅拌反应5h,最后将反应液温度降低至5℃,静置10h,得到聚酰亚胺前驱体溶液;2. In a nitrogen atmosphere, at a temperature of 5°C and under stirring conditions, add 3218.88g of water and 402.36g of N,N-dimethylacetamide into the three-necked flask, and then add 108.14g of p-phenylenediamine (1mol ), to obtain the reaction solution, 294.22g of 3,3,4',4'-biphenyltetracarboxylic dianhydride (1mol) was added to the reaction solution in three times by mass average, reacted for 5h, and then the reaction solution was heated to 20 DEG C, under nitrogen atmosphere, temperature is 20 DEG C and under stirring condition, add the diethanol monoisopropanolamine (0.025mol) of 4.08g, the dimethylcarbamoyl chloride (0.025mol) of 2.69g and 1.08g of NS-100, stirred and reacted for 5h, and finally lowered the temperature of the reaction solution to 5°C, and stood still for 10h to obtain a polyimide precursor solution;

利用上述一种聚酰亚胺前驱体溶液制备聚酰亚胺薄膜的方法是按以下步骤进行:The method that utilizes above-mentioned a kind of polyimide precursor solution to prepare polyimide film is to carry out as follows:

一、将聚酰亚胺前驱体溶液过滤并脱气,沿着T型狭缝流延到不锈钢制转鼓上,然后在温度为120℃下,干燥10min,得到自支撑薄膜;1. Filter and degas the polyimide precursor solution, cast it onto a stainless steel drum along the T-shaped slit, and then dry it at 120°C for 10 minutes to obtain a self-supporting film;

二、将自支撑薄膜从不锈钢制转鼓上剥离并置于固化炉中固化,首先在温度为150℃的条件下,加热3min,再在温度为250℃的条件下,加热3min,然后在温度为400℃的条件下,加热70s,最后在温度为300℃的条件下,退火处理约1min,得到聚酰亚胺薄膜;2. Peel the self-supporting film from the stainless steel drum and place it in a curing furnace for curing. First, heat it for 3 minutes at a temperature of 150°C, then heat it for 3 minutes at a temperature of 250°C, and then heat it at a temperature of 250°C. Heating at 400°C for 70s, and finally annealing at 300°C for about 1 min to obtain a polyimide film;

且固化过程中利用夹具夹持自支撑薄膜,使得自支撑薄膜固化前后纵向长度变化百分率为5%,横向长度变化百分率为20%。And during the curing process, the self-supporting film is clamped by a clamp, so that the percentage change of the longitudinal length of the self-supporting film before and after curing is 5%, and the percentage change of the transverse length is 20%.

本实施例制备的聚酰亚胺薄膜的厚度为25微米。The thickness of the polyimide film prepared in this embodiment is 25 microns.

对比实验一:Comparative experiment one:

一种聚酰亚胺前驱体溶液由叔胺、芳香二酐、芳香二胺及水制成;A polyimide precursor solution is made of tertiary amine, aromatic dianhydride, aromatic diamine and water;

所述的芳香二胺与叔胺的摩尔比为1:0.05;所述的芳香二胺与芳香二酐的摩尔比为1:1;所述的芳香二酐和芳香二胺的总质量与水的质量比为1:9;The molar ratio of the aromatic diamine to the tertiary amine is 1:0.05; the molar ratio of the aromatic diamine to the aromatic dianhydride is 1:1; the total mass of the aromatic dianhydride and the aromatic diamine to water The mass ratio is 1:9;

所述的芳香二胺为对苯二胺;Described aromatic diamine is p-phenylenediamine;

所述的叔胺为三乙基胺;Described tertiary amine is triethylamine;

所述的芳香二酐为3,3,4′,4′-联苯四羧酸二酐,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:The aromatic dianhydride is 3,3,4′,4′-biphenyltetracarboxylic dianhydride, and the repeating unit of polyamic acid in the polyimide precursor solution is:

上述一种聚酰亚胺前驱体溶液的制备方法是按以下步骤进行:The preparation method of above-mentioned a kind of polyimide precursor solution is to carry out as follows:

一、取5.06g的三乙基胺(0.05mol)、294.22g的3,3,4’,4’-联苯四羧酸二酐(1mol)、108.14g的对苯二胺(1mol)及3621.24g的水;1. Take 5.06g of triethylamine (0.05mol), 294.22g of 3,3,4',4'-biphenyltetracarboxylic dianhydride (1mol), 108.14g of p-phenylenediamine (1mol) and 3621.24g of water;

二、在氮气气氛、温度为5℃及搅拌条件下,向三颈瓶中加入3621.24g的水,然后加入108.14g的对苯二胺(1mol),得到反应液,将294.22g的3,3,4’,4’-联苯四羧酸二酐(1mol)按质量平均分三次加入到反应液中,反应5h,然后将反应液升温至20℃,在氮气气氛、温度为20℃及搅拌条件下,向反应液中加入5.06g的三乙基胺(0.05mol),搅拌反应5h,最后将反应液温度降低至5℃,静置10h,得到聚酰亚胺前驱体溶液;2. In a nitrogen atmosphere, at a temperature of 5°C and under stirring conditions, add 3621.24g of water to the three-necked flask, then add 108.14g of p-phenylenediamine (1mol) to obtain a reaction solution, and 294.22g of 3,3 , 4',4'-biphenyltetracarboxylic dianhydride (1mol) was added to the reaction liquid in three times according to the mass average, reacted for 5h, and then the reaction liquid was heated to 20°C, in a nitrogen atmosphere, the temperature was 20°C and stirred Under certain conditions, 5.06 g of triethylamine (0.05 mol) was added to the reaction solution, stirred and reacted for 5 hours, and finally the temperature of the reaction solution was lowered to 5° C., and allowed to stand for 10 hours to obtain a polyimide precursor solution;

利用上述一种聚酰亚胺前驱体溶液制备聚酰亚胺薄膜的方法是按以下步骤进行:The method that utilizes above-mentioned a kind of polyimide precursor solution to prepare polyimide film is to carry out as follows:

一、将聚酰亚胺前驱体溶液过滤并脱气,沿着T型狭缝流延到不锈钢制转鼓上,然后在温度为120℃下,干燥10min,得到自支撑薄膜;1. Filter and degas the polyimide precursor solution, cast it onto a stainless steel drum along the T-shaped slit, and then dry it at 120°C for 10 minutes to obtain a self-supporting film;

二、将自支撑薄膜从不锈钢制转鼓上剥离并置于固化炉中,在温度为150℃的条件下固化,固化过程中利用夹具夹持自支撑薄膜,牵引加热下自支撑膜发生断裂,断裂时纵向伸长率在5%,得到聚酰亚胺薄。2. The self-supporting film is peeled off from the stainless steel drum and placed in a curing furnace, and cured at a temperature of 150 ° C. During the curing process, the self-supporting film is clamped by a clamp, and the self-supporting film breaks under traction and heating. The longitudinal elongation at break is 5%, and the obtained polyimide is thin.

对比实验一无法得到连续的聚酰亚胺薄膜。In comparative experiment 1, a continuous polyimide film could not be obtained.

对比实验二:Comparative experiment two:

一种聚酰亚胺前驱体溶液由叔胺、水性脱模剂、芳香二酐、芳香二胺及水制成;A polyimide precursor solution is made of tertiary amine, aqueous release agent, aromatic dianhydride, aromatic diamine and water;

所述的芳香二胺与叔胺的摩尔比为1:0.05;所述的芳香二胺与水性脱模剂的质量比为1:0.01;所述的芳香二胺与芳香二酐的摩尔比为1:1;所述的芳香二酐和芳香二胺的总质量与水的质量比为1:9;The molar ratio of the aromatic diamine to the tertiary amine is 1:0.05; the mass ratio of the aromatic diamine to the aqueous release agent is 1:0.01; the molar ratio of the aromatic diamine to the aromatic dianhydride is 1:1; the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to water is 1:9;

所述的芳香二胺为对苯二胺;Described aromatic diamine is p-phenylenediamine;

所述的叔胺为二乙醇单异丙醇胺;Described tertiary amine is diethanol monoisopropanolamine;

所述的水性脱模剂为日本山一化学公司生产的NS-100;The water-based release agent is NS-100 produced by Japan Yamaichi Chemical Company;

所述的芳香二酐为3,3,4′,4′-联苯四羧酸二酐,所述的聚酰亚胺前驱体溶液中封端的聚酰胺酸的重复单元为:The aromatic dianhydride is 3,3,4′,4′-biphenyltetracarboxylic dianhydride, and the repeating unit of the polyamic acid blocked in the polyimide precursor solution is:

上述一种聚酰亚胺前驱体溶液的制备方法是按以下步骤进行:The preparation method of above-mentioned a kind of polyimide precursor solution is to carry out as follows:

一、取8.16g的二乙醇单异丙醇胺(0.05mol)、1.08g的NS-100、294.22g的3,3,4’,4’-联苯四羧酸二酐(1mol)、108.14g的对苯二胺(1mol)及3621.24g的水;1. Take 8.16g of diethanol monoisopropanolamine (0.05mol), 1.08g of NS-100, 294.22g of 3,3,4',4'-biphenyltetracarboxylic dianhydride (1mol), 108.14 g of p-phenylenediamine (1mol) and 3621.24g of water;

二、在氮气气氛、温度为5℃及搅拌条件下,向三颈瓶中加入3621.24g的水,然后加入108.14g的对苯二胺(1mol),得到反应液,将294.22g的3,3,4’,4’-联苯四羧酸二酐(1mol)按质量平均分三次加入到反应液中,反应5h,然后将反应液升温至20℃,在氮气气氛、温度为20℃及搅拌条件下,向反应液中加入8.16g的二乙醇单异丙醇胺(0.05mol)和1.08g的NS-100,搅拌反应5h,最后将反应液温度降低至5℃,静置10h,得到聚酰亚胺前驱体溶液;2. In a nitrogen atmosphere, at a temperature of 5°C and under stirring conditions, add 3621.24g of water to the three-necked flask, then add 108.14g of p-phenylenediamine (1mol) to obtain a reaction solution, and 294.22g of 3,3 , 4',4'-biphenyltetracarboxylic dianhydride (1mol) was added to the reaction liquid in three times according to the mass average, reacted for 5h, and then the reaction liquid was heated to 20°C, in a nitrogen atmosphere, the temperature was 20°C and stirred Under certain conditions, 8.16 g of diethanol monoisopropanolamine (0.05 mol) and 1.08 g of NS-100 were added to the reaction liquid, and the reaction was stirred for 5 hours. Finally, the temperature of the reaction liquid was lowered to 5° C. and allowed to stand for 10 hours to obtain poly Imide precursor solution;

利用上述一种聚酰亚胺前驱体溶液制备聚酰亚胺薄膜的方法是按以下步骤进行:The method that utilizes above-mentioned a kind of polyimide precursor solution to prepare polyimide film is to carry out as follows:

一、将聚酰亚胺前驱体溶液过滤并脱气,沿着T型狭缝流延到不锈钢制转鼓上,然后在温度为120℃下,干燥10min,得到自支撑薄膜;1. Filter and degas the polyimide precursor solution, cast it onto a stainless steel drum along the T-shaped slit, and then dry it at 120°C for 10 minutes to obtain a self-supporting film;

二、将自支撑薄膜从不锈钢制转鼓上剥离并置于固化炉中固化,固化过程中利用夹具夹持自支撑薄膜,在温度为150℃的条件下固化3min,然后在温度为250℃的条件下牵引加热过程中自支撑膜发生断裂,断裂时纵向伸长率在8%,得到聚酰亚胺薄。2. Peel the self-supporting film from the stainless steel drum and place it in a curing oven for curing. During the curing process, use a clamp to hold the self-supporting film, and cure it at a temperature of 150°C for 3 minutes, and then place it in a curing oven at a temperature of 250°C. Under certain conditions, the self-supporting film breaks during the traction heating process, and the longitudinal elongation at breakage is 8%, and the polyimide film is obtained.

对比实验二无法得到连续的聚酰亚胺薄膜。In comparative experiment 2, a continuous polyimide film could not be obtained.

对实施例一及五制备的聚酰亚胺薄膜及对比实验一及二制备的聚酰亚胺薄的表面质量,通过表面微裂纹、表面平整度、表面气泡方式进行评价。The surface quality of the polyimide films prepared in Examples 1 and 5 and the polyimide films prepared in Comparative Experiments 1 and 2 were evaluated by means of surface microcracks, surface smoothness, and surface air bubbles.

①、表面微裂纹:①. Micro-cracks on the surface:

评价聚酰亚胺薄膜表面的微裂纹,评价标准如下:Evaluate the micro-cracks on the polyimide film surface, the evaluation criteria are as follows:

A:未发现薄膜表面存在微裂纹;A: No microcracks were found on the surface of the film;

B:在薄膜的表面(小于膜表面积的5%)上可以确认存在表面微裂纹;B: on the surface of the film (less than 5% of the film surface area), it can be confirmed that there are surface microcracks;

C:在薄膜的表面(大于膜表面积的5%、小于10%)上可以确认存在表面微裂纹;C: on the surface of the film (greater than 5%, less than 10% of the film surface area), it can be confirmed that there are surface microcracks;

D:在薄膜的表面(大于膜表面积的10%)上可以确认存在表面微裂纹。D: The presence of surface microcracks can be confirmed on the surface of the film (more than 10% of the film surface area).

②、表面平整度:②. Surface roughness:

评价聚酰亚胺薄膜的表面平整度,评价标准如下:Evaluate the surface smoothness of polyimide film, evaluation standard is as follows:

A:采用螺旋测微器对薄膜的厚度进行测试,取不同区域(每个区域占单位幅宽表面积的比例不少于15%)的5个测试点数据,得到数据的最大值、最小值减去平均值,与平均值的比例均在±5%以内;A: Use a spiral micrometer to test the thickness of the film, take the data of 5 test points in different areas (each area accounts for no less than 15% of the surface area per unit width), and obtain the maximum value, minimum value and minus value of the data. Remove the average value, and the ratio to the average value is within ±5%;

B:采用螺旋测微器对薄膜的厚度进行测试,取不同区域(每个区域占单位幅宽表面积的比例不少于15%)的5个测试点数据,得到数据的最大值、最小值减去平均值,与平均值的比例均在±10%以内;B: Use a spiral micrometer to test the thickness of the film, take data from 5 test points in different regions (each region accounts for no less than 15% of the surface area per unit width), and obtain the maximum value, minimum value minus the value of the data. Remove the average value, and the ratio to the average value is within ±10%;

C:采用螺旋测微器对薄膜的厚度进行测试,取不同区域(每个区域占单位幅宽表面积的比例不少于15%)的5个测试点数据,得到数据的最大值、最小值减去平均值,与平均值的比例均在±15%以内;C: Use a spiral micrometer to test the thickness of the film, take the data of 5 test points in different regions (each region accounts for no less than 15% of the surface area per unit width), and obtain the maximum value, minimum value minus the value of the data. Remove the average value, and the ratio to the average value is within ±15%;

D:采用螺旋测微器对薄膜的厚度进行测试,取不同区域(每个区域占单位幅宽表面积的比例不少于15%)的5个测试点数据,得到数据的最大值、最小值减去平均值,与平均值的比例均在±15%以外。D: Use a spiral micrometer to test the thickness of the film, take the data of 5 test points in different regions (each region accounts for no less than 15% of the surface area per unit width), and obtain the maximum value, minimum value minus the value of the data. The average value is removed, and the ratio to the average value is outside ±15%.

③、表面气泡:③. Surface bubbles:

评价聚酰亚胺薄膜表面存在的表面气泡,评价标准如下:Evaluate the surface air bubble that polyimide film surface exists, evaluation standard is as follows:

A:聚酰亚胺薄膜表面不存在表面气泡;A: there is no surface bubble on the surface of the polyimide film;

B:聚酰亚胺薄膜表面(10cm X 10cm)存在的表面气泡多于1个但是少于5个;B: the surface bubble that exists on polyimide film surface (10cm * 10cm) is more than 1 but less than 5;

C:聚酰亚胺薄膜表面(10cm X 10cm)存在的表面气泡多于5个但是少于50个;C: the surface bubbles that exist on the polyimide film surface (10cm * 10cm) are more than 5 but less than 50;

D:聚酰亚胺薄膜表面(10cm X 10cm)存在的表面气泡多于50个。D: there are more than 50 surface bubbles on the polyimide film surface (10cm * 10cm).

对实施例一及五制备的聚酰亚胺薄膜及对比实验一及二制备的聚酰亚胺薄膜测试5%热失重温度:测试采用热失重分析仪(TGA)。升温速率:10℃/min;测试气氛:空气。The 5% thermal weight loss temperature was measured for the polyimide films prepared in Examples 1 and 5 and the polyimide films prepared in Comparative Experiments 1 and 2: the test was performed using a thermogravimetric analyzer (TGA). Heating rate: 10°C/min; Test atmosphere: air.

对实施例一及五制备的聚酰亚胺薄膜及对比实验一及二制备的聚酰亚胺薄膜测试800%残炭率:测试采用热失重分析仪(TGA)。升温速率:10℃/min;测试气氛:氮气。The polyimide films prepared in Examples 1 and 5 and the polyimide films prepared in Comparative Experiments 1 and 2 were tested for 800% carbon residue rate: the test was performed using a thermogravimetric analyzer (TGA). Heating rate: 10°C/min; test atmosphere: nitrogen.

对实施例一及五制备的聚酰亚胺薄膜及对比实验一及二制备的聚酰亚胺薄膜测试玻璃化转变温度:测试采用动态热机械分析仪(DMA)。升温速率:5℃/min;测试气氛:空气。The glass transition temperature of the polyimide films prepared in Examples 1 and 5 and the polyimide films prepared in Comparative Experiments 1 and 2 was tested: a dynamic thermomechanical analyzer (DMA) was used for the test. Heating rate: 5°C/min; Test atmosphere: air.

对实施例一及五制备的聚酰亚胺薄膜及对比实验一及二制备的聚酰亚胺薄膜进行力学测试,采用ASTM D882标准进行测试。Mechanical tests were performed on the polyimide films prepared in Examples 1 and 5 and the polyimide films prepared in Comparative Experiments 1 and 2, using the ASTM D882 standard for testing.

表1为聚酰亚胺薄膜表面质量和成膜性,表2为连续制备聚酰亚胺薄膜性能。由表1可知,对比实验无法完成连续化聚酰亚胺薄膜制备,在固化炉操作中发生不可逆的自支撑膜断裂,纵向伸长率没有达到标准,同时尚未进行横向伸长操作。此外,对比实验在表面质量方面均远低于实施例,包括表面平整度、表面微裂纹和表面气泡方面均差于实施例。其中,实施例四和实施例五,由于采用了多种胺类催化剂复合高沸点溶剂,使得形成的薄膜,相比于实施例一至三,具有更为优异的表面平整度。Table 1 is the surface quality and film-forming properties of polyimide films, and Table 2 is the performance of continuously prepared polyimide films. It can be seen from Table 1 that the continuous polyimide film preparation cannot be completed in the comparative experiment, irreversible self-supporting film fracture occurred during the operation of the curing oven, the longitudinal elongation did not meet the standard, and the transverse elongation operation has not yet been performed. In addition, the comparative experiments are far lower than the examples in terms of surface quality, including surface flatness, surface microcracks and surface air bubbles. Among them, in Embodiment 4 and Embodiment 5, due to the use of multiple amine catalysts combined with high boiling point solvents, the formed film has a more excellent surface smoothness than Embodiments 1 to 3.

由表2可知,对比实验由于无法完成连续化薄膜制备。所以不能测试薄膜的力学性能(ND),只对部分样品进行了热性能测试。由测试可知,对比试验的热性能数据均低于实施例,是由于没有采用适宜的伸长取向,对聚酰亚胺材料的热性能造成一定影响。对比实施例五和实施例四,同样是由于没有适宜的面内双向的伸长取向,对薄膜的热性能和机械性能都造成的影响,尤其是力学性能。It can be seen from Table 2 that the continuous thin film preparation cannot be completed in the comparative experiment. Therefore, the mechanical properties (ND) of the films could not be tested, and only some samples were tested for thermal properties. It can be seen from the test that the thermal performance data of the comparative tests are all lower than those of the examples, because the thermal performance of the polyimide material is affected to some extent due to the lack of proper elongation orientation. Comparing Example 5 and Example 4, it is also because there is no suitable in-plane bidirectional elongation orientation, which affects both the thermal and mechanical properties of the film, especially the mechanical properties.

图1为实施例四制备的聚酰亚胺薄膜照片;图2为对比实验一制备的聚酰亚胺薄膜照片。从图可知,对比试验得到的聚酰亚胺薄膜表面质量不好,同时由于薄膜中途脆断,无法进行横向拉伸,导致薄膜表面出现褶皱,端部出现断裂纹路。Fig. 1 is the photo of the polyimide film prepared in Example 4; Fig. 2 is the photo of the polyimide film prepared in Comparative Experiment 1. It can be seen from the figure that the surface quality of the polyimide film obtained in the comparison test is not good, and at the same time, because the film is brittle and broken midway, it cannot be stretched transversely, resulting in wrinkles on the film surface and fracture lines at the end.

表1 聚酰亚胺薄膜表面质量和成膜性Table 1 Surface quality and film-forming properties of polyimide films

表2 连续制备的聚酰亚胺薄膜性能Table 2 Properties of polyimide films prepared continuously

Claims (10)

1.一种聚酰亚胺前驱体溶液,其特征在于一种聚酰亚胺前驱体溶液由叔胺、水性脱模剂、芳香二酐、芳香二胺、极性溶剂及水制成;1. A polyimide precursor solution is characterized in that a polyimide precursor solution is made of tertiary amine, aqueous release agent, aromatic dianhydride, aromatic diamine, polar solvent and water; 所述的芳香二胺与叔胺的摩尔比为1:(0.05~1.5);所述的芳香二胺与水性脱模剂的质量比为1:(0.01~1);所述的芳香二胺与芳香二酐的摩尔比为1:(0.97~1.03);所述的芳香二酐和芳香二胺的总质量与水的质量比为1:(2~10);所述的芳香二酐和芳香二胺的总质量与极性溶剂的质量比为1:(0~10);The molar ratio of the aromatic diamine to the tertiary amine is 1:(0.05~1.5); the mass ratio of the aromatic diamine to the aqueous release agent is 1:(0.01~1); the aromatic diamine The molar ratio to aromatic dianhydride is 1:(0.97~1.03); the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to water is 1:(2~10); the aromatic dianhydride and The mass ratio of the total mass of aromatic diamine to the polar solvent is 1:(0~10); 所述的芳香二胺为4,4′-二氨基二苯醚、4,4′-二氨基二苯甲烷、二(3-氨基苯氧基)二苯甲酮、对苯二胺、间苯二胺和4,4′-二氨基二苯砜中的一种或其中几种的混合物;The aromatic diamines are 4,4'-diaminodiphenyl ether, 4,4'-diaminodiphenylmethane, bis(3-aminophenoxy)benzophenone, p-phenylenediamine, m-phenylenediamine One or a mixture of diamines and 4,4'-diaminodiphenylsulfone; 所述的叔胺为低沸点叔胺或低沸点叔胺与高沸点叔胺的混合物,所述的低沸点叔胺与高沸点叔胺的摩尔比例为1:(0.01~100);所述的低沸点叔胺为沸点在150℃以下,且低沸点叔胺的分子量为80g/mol~250g/mol;所述的高沸点叔胺为沸点在150℃~295℃的叔胺;The tertiary amine is a low-boiling tertiary amine or a mixture of a low-boiling tertiary amine and a high-boiling tertiary amine, and the molar ratio of the low-boiling tertiary amine to the high-boiling tertiary amine is 1:(0.01-100); the The low-boiling point tertiary amine has a boiling point below 150°C, and the molecular weight of the low-boiling point tertiary amine is 80g/mol-250g/mol; the high-boiling point tertiary amine is a tertiary amine with a boiling point between 150°C-295°C; 所述的极性溶剂为N,N-二甲基乙酰胺、N,N-二甲基甲酰胺、乙二醇和二甲基亚砜中的一种或其中几种的混合物;The polar solvent is one of N,N-dimethylacetamide, N,N-dimethylformamide, ethylene glycol and dimethyl sulfoxide or a mixture of several of them; 当所述的芳香二酐为3,3,4′,4′-二苯醚四羧酸二酐、3,3,4′,4′-二砜基四羧酸二酐或3,3,4′,4′-二苯甲酮四羧酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride is 3,3,4',4'-diphenyl ether tetracarboxylic dianhydride, 3,3,4',4'-disulfone tetracarboxylic dianhydride or 3,3, 4',4'-benzophenone tetracarboxylic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is: 所述的R1为-O-或 The R 1 is -O- or 所述的R2 The R2 is 当所述的芳香二酐为3,3,4′,4′-联苯四羧酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride is 3,3,4′,4′-biphenyltetracarboxylic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is: 所述的R3 The R3 is 当所述的芳香二酐为均苯四甲酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride is pyromellitic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is: 所述的R4 The R 4 is 2.根据权利要求1所述的一种聚酰亚胺前驱体溶液,其特征在于所述的低沸点叔胺为三乙基胺、十二烷基二甲基叔胺、二乙醇单异丙醇胺和甲基吡啶中的一种或其中几种的混合物。2. a kind of polyimide precursor solution according to claim 1, it is characterized in that described low boiling point tertiary amine is triethylamine, dodecyl dimethyl tertiary amine, diethanol monoisopropyl One or a mixture of alcohol amines and picoline. 3.根据权利要求1所述的一种聚酰亚胺前驱体溶液,其特征在于所述的高沸点叔胺为三正丁胺、三异丙醇胺和二甲胺基甲酰氯中的一种或其中几种的混合物。3. a kind of polyimide precursor solution according to claim 1, it is characterized in that described high boiling point tertiary amine is one in tri-n-butylamine, triisopropanolamine and dimethylcarbamoyl chloride species or a mixture of several of them. 4.根据权利要求1所述的一种聚酰亚胺前驱体溶液,其特征在于所述的水性脱模剂为在温度小于100℃的条件下能与水互溶,且不析出的脱模剂或离型剂。4. A kind of polyimide precursor solution according to claim 1, it is characterized in that described aqueous release agent is the release agent that can be miscible with water under the condition that temperature is less than 100 ℃, and does not separate out or release agent. 5.如权利要求1所述的一种聚酰亚胺前驱体溶液的制备方法,其特征在于一种聚酰亚胺前驱体溶液的制备方法是按以下步骤进行:5. the preparation method of a kind of polyimide precursor solution as claimed in claim 1 is characterized in that the preparation method of a kind of polyimide precursor solution is to carry out according to the following steps: 一、取叔胺、水性脱模剂、芳香二酐、芳香二胺、极性溶剂及水;1. Take tertiary amine, water-based release agent, aromatic dianhydride, aromatic diamine, polar solvent and water; 所述的芳香二胺与叔胺的摩尔比为1:(0.05~1.5);所述的芳香二胺与水性脱模剂的质量比为1:(0.01~1);所述的芳香二胺与芳香二酐的摩尔比为1:(0.97~1.03);所述的芳香二酐和芳香二胺的总质量与水的质量比为1:(2~10);所述的芳香二酐和芳香二胺的总质量与极性溶剂的质量比为1:(0~10);The molar ratio of the aromatic diamine to the tertiary amine is 1:(0.05~1.5); the mass ratio of the aromatic diamine to the aqueous release agent is 1:(0.01~1); the aromatic diamine The molar ratio to aromatic dianhydride is 1:(0.97~1.03); the mass ratio of the total mass of the aromatic dianhydride and aromatic diamine to water is 1:(2~10); the aromatic dianhydride and The mass ratio of the total mass of aromatic diamine to the polar solvent is 1:(0~10); 二、在氮气气氛、温度为2℃~10℃及搅拌条件下,向三颈瓶中加入步骤一中称取的水和极性溶剂,然后加入步骤一中称取的芳香二胺,得到反应液,将步骤一中称取的芳香二酐按质量平均分三次加入到反应液中,反应1h~5h,然后将反应液升温至20℃~60℃,在氮气气氛、温度为20℃~60℃及搅拌条件下,向反应液中加入步骤一中称取的叔胺和水性脱模剂,搅拌反应3h~5h,最后将反应液温度降低至2℃~10℃,静置1h~10h,得到聚酰亚胺前驱体溶液;2. In a nitrogen atmosphere, at a temperature of 2°C to 10°C and under stirring conditions, add the water and polar solvent weighed in step 1 to the three-necked flask, and then add the aromatic diamine weighed in step 1 to obtain the reaction solution, the aromatic dianhydride weighed in step 1 was added to the reaction solution in three equal parts by mass, reacted for 1h to 5h, and then the reaction solution was heated to 20°C to 60°C, in a nitrogen atmosphere, the temperature was 20°C to 60°C ℃ and under stirring conditions, add the tertiary amine and water-based release agent weighed in step 1 to the reaction solution, stir and react for 3h to 5h, and finally reduce the temperature of the reaction solution to 2℃~10℃, and let it stand for 1h~10h. Obtain polyimide precursor solution; 步骤一中所述的芳香二胺为4,4′-二氨基二苯醚、4,4′-二氨基二苯甲烷、二(3-氨基苯氧基)二苯甲酮、对苯二胺、间苯二胺和4,4′-二氨基二苯砜中的一种或其中几种的混合物;The aromatic diamine described in step 1 is 4,4'-diaminodiphenyl ether, 4,4'-diaminodiphenylmethane, bis(3-aminophenoxy)benzophenone, p-phenylenediamine , m-phenylenediamine and 4,4'-diaminodiphenyl sulfone or a mixture of several of them; 步骤一中所述的叔胺为低沸点叔胺或低沸点叔胺与高沸点叔胺的混合物,所述的低沸点叔胺与高沸点叔胺的摩尔比例为1:(0.01~100);所述的低沸点叔胺为沸点在150℃以下,且低沸点叔胺的分子量为80g/mol~250g/mol;所述的高沸点叔胺为沸点在150℃~295℃的叔胺;The tertiary amine described in step 1 is a low-boiling tertiary amine or a mixture of a low-boiling tertiary amine and a high-boiling tertiary amine, and the molar ratio of the low-boiling tertiary amine to the high-boiling tertiary amine is 1:(0.01~100); The low-boiling tertiary amine has a boiling point below 150°C, and the molecular weight of the low-boiling tertiary amine is 80g/mol-250g/mol; the high-boiling tertiary amine is a tertiary amine with a boiling point of 150°C-295°C; 步骤一中所述的极性溶剂为N,N-二甲基乙酰胺、N,N-二甲基甲酰胺、乙二醇和二甲基亚砜中的一种或其中几种的混合物;The polar solvent described in step 1 is one or a mixture of several of N,N-dimethylacetamide, N,N-dimethylformamide, ethylene glycol and dimethyl sulfoxide; 当步骤一中所述的芳香二酐为3,3,4′,4′-二苯醚四羧酸二酐、3,3,4′,4′-二砜基四羧酸二酐或3,3,4′,4′-二苯甲酮四羧酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride described in step 1 is 3,3,4',4'-diphenyl ether tetracarboxylic dianhydride, 3,3,4',4'-disulfone tetracarboxylic dianhydride or 3 , 3,4',4'-benzophenone tetracarboxylic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is: 所述的R1为-O-或 The R 1 is -O- or 所述的R2 The R2 is 当步骤一中所述的芳香二酐为3,3,4′,4′-联苯四羧酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride described in step 1 is 3,3,4′,4′-biphenyltetracarboxylic dianhydride, the repeating unit of polyamic acid in the polyimide precursor solution is: 所述的R3 The R3 is 当步骤一中所述的芳香二酐为均苯四甲酸二酐时,所述的聚酰亚胺前驱体溶液中聚酰胺酸的重复单元为:When the aromatic dianhydride described in step 1 is pyromellitic dianhydride, the repeating unit of polyamic acid in the described polyimide precursor solution is: 所述的R4 The R 4 is 6.根据权利要求5所述的一种聚酰亚胺前驱体溶液的制备方法,其特征在于步骤一中所述的低沸点叔胺为三乙基胺、十二烷基二甲基叔胺、二乙醇单异丙醇胺和甲基吡啶中的一种或其中几种的混合物。6. the preparation method of a kind of polyimide precursor solution according to claim 5 is characterized in that the low boiling point tertiary amine described in step 1 is triethylamine, dodecyl dimethyl tertiary amine , diethanol monoisopropanolamine and picoline or a mixture of several of them. 7.根据权利要求5所述的一种聚酰亚胺前驱体溶液的制备方法,其特征在于步骤一中所述的高沸点叔胺为三正丁胺、三异丙醇胺和二甲胺基甲酰氯中的一种或其中几种的混合物。7. the preparation method of a kind of polyimide precursor solution according to claim 5 is characterized in that the high boiling point tertiary amine described in step 1 is tri-n-butylamine, triisopropanolamine and dimethylamine One or a mixture of several of the methanoyl chlorides. 8.根据权利要求5所述的一种聚酰亚胺前驱体溶液的制备方法,其特征在于步骤一中所述的水性脱模剂为在温度小于100℃的条件下能与水互溶,且不析出的脱模剂或离型剂。8. The preparation method of a kind of polyimide precursor solution according to claim 5, it is characterized in that the water-based release agent described in step 1 can be miscible with water under the condition that the temperature is less than 100 ℃, and Mold release or release agent that does not precipitate. 9.利用权利要求1所述的一种聚酰亚胺前驱体溶液制备聚酰亚胺薄膜的方法,其特征在于利用一种聚酰亚胺前驱体溶液制备聚酰亚胺薄膜的方法是按以下步骤进行:9. utilize a kind of polyimide precursor solution described in claim 1 to prepare the method for polyimide film, it is characterized in that utilizing a kind of polyimide precursor solution to prepare the method for polyimide film is to press Follow these steps: 一、将聚酰亚胺前驱体溶液过滤并脱气,沿着T型狭缝流延到不锈钢制转鼓上,然后在温度为60℃~180℃下,干燥1min~50min,得到自支撑薄膜;1. Filter and degas the polyimide precursor solution, cast it on a stainless steel drum along the T-shaped slit, and then dry it at a temperature of 60 ° C to 180 ° C for 1 min to 50 min to obtain a self-supporting film ; 二、将自支撑薄膜从不锈钢制转鼓上剥离并置于固化炉中固化,首先在温度为150℃~200℃的条件下,加热1min~60min,再在温度为200℃~250℃的条件下,加热1min~60min,然后在温度为250℃~450℃的条件下,加热1min~60min,最后在温度为290℃~310℃的条件下,退火处理约1min~20min,得到聚酰亚胺薄膜;2. Peel the self-supporting film from the stainless steel drum and place it in a curing furnace for curing. First, heat it for 1min to 60min at a temperature of 150°C to 200°C, and then heat it at a temperature of 200°C to 250°C. , heating for 1min to 60min, then heating for 1min to 60min at a temperature of 250°C to 450°C, and finally annealing for about 1min to 20min at a temperature of 290°C to 310°C to obtain polyimide film; 且固化过程中利用夹具夹持自支撑薄膜,使得自支撑薄膜固化前后纵向长度变化百分率为5%~20%,横向长度变化百分率为10%~80%。And during the curing process, the self-supporting film is clamped by a clamp, so that the percentage change of the longitudinal length of the self-supporting film before and after curing is 5%-20%, and the percentage change of the transverse length is 10%-80%. 10.根据权利要求9所述的利用一种聚酰亚胺前驱体溶液制备聚酰亚胺薄膜的方法,其特征在于步骤一中然后在温度为80℃~160℃下,干燥10min~30min。10 . The method for preparing a polyimide film by using a polyimide precursor solution according to claim 9 , wherein in step 1, drying is performed at a temperature of 80° C. to 160° C. for 10 minutes to 30 minutes. 11 .
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