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CN111019129A - Low-thermal expansion coefficient soluble polyimide resin powder and preparation method thereof - Google Patents

Low-thermal expansion coefficient soluble polyimide resin powder and preparation method thereof Download PDF

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CN111019129A
CN111019129A CN201911154043.4A CN201911154043A CN111019129A CN 111019129 A CN111019129 A CN 111019129A CN 201911154043 A CN201911154043 A CN 201911154043A CN 111019129 A CN111019129 A CN 111019129A
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thermal expansion
expansion coefficient
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姬亚宁
白小庆
冯婷婷
青双桂
蒋耿杰
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Guilin Electrical Equipment Scientific Research Institute Co Ltd
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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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
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    • C08G73/1067Wholly aromatic polyimides, i.e. having both tetracarboxylic and diamino moieties aromatically bound
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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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    • C08G73/06Polycondensates having nitrogen-containing heterocyclic rings in the main chain of the macromolecule
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Abstract

The invention discloses a soluble polyimide resin powder with low thermal expansion coefficient and a preparation method thereof. The preparation method of the low-thermal expansion coefficient soluble polyimide resin powder comprises the following steps: firstly, 4 '-diamino-2, 2' -bistrifluoromethylbiphenyl reacts with dianhydride monomer with a limited structure in an aprotic polar solvent to obtain a segmented polyamic acid resin solution; adding diamine monomer and non-proton polar solvent with limited structure, and then adding dianhydride monomer with limited structure in batches for reaction to obtain soluble polyamic acid resin solution with low thermal expansion coefficient; finally, imidizing the obtained solution to obtain the soluble polyimide resin powder with low thermal expansion coefficient. The polyimide resin powder can be dissolved in polar solvents such as DMAc, NMP, toluene, cyclohexanone and the like, has a low thermal expansion coefficient, is close to a metal copper foil, and has a more valuable application prospect in electronic components.

Description

一种低热膨胀系数可溶性聚酰亚胺树脂粉及其制备方法A kind of low thermal expansion coefficient soluble polyimide resin powder and preparation method thereof

技术领域technical field

本发明涉及聚酰亚胺材料,具体涉及一种低热膨胀系数可溶性聚酰亚胺树脂粉及其制备方法。The invention relates to polyimide materials, in particular to a low thermal expansion coefficient soluble polyimide resin powder and a preparation method thereof.

背景技术Background technique

聚酰亚胺(PI)以其具有优异的耐高温性、机械性能、耐药品性能,被广泛应用在电子电工行业领域,但因其本身固有的不溶不熔特性,使其加工成型困难,限制了应用范围。目前为止,已有不少文献报道通过采用在聚酰亚胺分子结构中引入柔性链段、扭曲链段、脂族链段等措施,可以将聚酰亚胺的加工温度降低到370℃,虽然可以加工,但是条件依然很苛刻,在块状成型品加工时易出现制品尺寸与标准件尺寸差别、内部有气泡等现象,造成制件成品率非常低。另一方面,国内模塑加工厂商大都采用传统的加工设备,主要用来加工聚烯烃类、环氧类等低温可加工树脂,设备最高使用温度仅能达到250℃,仍然不能对聚酰亚胺热加工成型。Polyimide (PI) is widely used in the field of electronic and electrical industry due to its excellent high temperature resistance, mechanical properties and chemical resistance properties, but its inherent insoluble and infusible properties make it difficult to process and form. The scope of application is limited. So far, many literatures have reported that the processing temperature of polyimide can be reduced to 370 °C by introducing flexible segments, twisted segments, and aliphatic segments into the molecular structure of polyimide. It can be processed, but the conditions are still very harsh. During the processing of block shaped products, the difference between the size of the product and the standard part, and the presence of air bubbles in the interior are prone to occur, resulting in a very low yield of the finished product. On the other hand, most domestic molding processing manufacturers use traditional processing equipment, which is mainly used to process low-temperature processable resins such as polyolefin and epoxy. Hot forming.

可溶性聚酰亚胺树脂是一种能溶解在极性溶剂(如二甲基乙酰胺或二甲基吡咯烷酮等)中,然后通过涂布或涂刷成型,再经低温干燥可得到的高强度高耐热材料,可应用在封装、密封、包封等方面。可溶性聚酰亚胺的设计思路是通过在聚酰亚胺分子主链中引入脂环结构、不对称结构、柔性基团、脂肪链等来降低聚酰亚胺自由体积密度,这种结构虽然可提高聚酰亚胺溶解性能,但却牺牲了其耐热性和尺寸稳定性。如公开号为CN103724623A的发明专利,提出一种可溶可熔的聚酰亚胺模塑粉,其玻璃化转变温度Tg为289~294℃、拉伸强度为114~120MPa,文中虽未提及其热膨胀系数(CTE),但本领域技术人员由其采用的单体主要包含2,3,3',4'-二苯醚四甲酸二酐与4,4'-二氨基二苯醚,较多的柔性基团醚键导致分子链较为柔软,导致其刚性不足,CTE偏高。而公开号为CN102369233A的发明专利,提出一种含有环己烷二胺与其它二胺(降冰片烯二胺)的组合作为聚酰亚胺的二胺成分,实现低热膨胀系数、高光透过率和高的紫外光透过率特性的聚酰亚胺树脂。该发明所述聚酰亚胺树脂CTE虽低至14ppm/K(取值区间100~200℃),但其所采用的环己二胺的价格昂贵,成本较高;另一方面,本领域技术人员由其采用的单体可知,其所得聚酰亚胺树脂不溶或难溶于非质子极性溶剂或其它有机溶剂(如甲苯、环己酮等),由此可见,要使所得聚酰亚胺树脂粉同时具有较低的CTE和较好的加工性是目前存在的技术难点。Soluble polyimide resin is a kind of high-strength and high-strength resin that can be dissolved in polar solvents (such as dimethylacetamide or dimethylpyrrolidone, etc.), then formed by coating or brushing, and then dried at low temperature. Heat-resistant materials can be used in packaging, sealing, encapsulation, etc. The design idea of soluble polyimide is to reduce the free bulk density of polyimide by introducing alicyclic structure, asymmetric structure, flexible group, aliphatic chain, etc. into the main chain of polyimide molecule. Improve the solubility of polyimide, but sacrifice its heat resistance and dimensional stability. For example, the invention patent with publication number CN103724623A proposes a soluble and fusible polyimide molding powder, whose glass transition temperature Tg is 289-294°C and tensile strength is 114-120MPa, although it is not mentioned in the text Its coefficient of thermal expansion (CTE), but the monomers used by those skilled in the art mainly include 2,3,3',4'-diphenyl ether tetracarboxylic dianhydride and 4,4'-diaminodiphenyl ether, more Too many flexible groups of ether bonds make the molecular chain relatively soft, resulting in insufficient rigidity and high CTE. The invention patent with publication number CN102369233A proposes a combination of cyclohexanediamine and other diamines (norbornene diamine) as the diamine component of polyimide to achieve low thermal expansion coefficient and high light transmittance. and high UV transmittance characteristics of polyimide resin. Although the CTE of the polyimide resin described in the invention is as low as 14ppm/K (the value range is 100-200°C), the cyclohexanediamine used is expensive and the cost is high; It can be known from the monomers used by the personnel that the polyimide resin obtained by it is insoluble or insoluble in aprotic polar solvents or other organic solvents (such as toluene, cyclohexanone, etc.). Amine resin powder has lower CTE and better processability at the same time, which is a technical difficulty at present.

发明内容SUMMARY OF THE INVENTION

本发明要解决的技术问题是针对现有低热膨胀系数聚酰亚胺树脂存在的加工性不足、可溶可熔聚酰亚胺刚性不足的问题,提供一种低热膨胀系数聚酰亚胺树脂粉及其制备方法The technical problem to be solved by the present invention is to provide a low thermal expansion coefficient polyimide resin powder for the problems of insufficient processability and insufficient rigidity of the soluble polyimide polyimide in the existing low thermal expansion coefficient polyimide resin. and preparation method thereof

为解决上述技术问题,本发明采用以下技术方案:In order to solve the above-mentioned technical problems, the present invention adopts the following technical solutions:

一种低热膨胀系数可溶性聚酰亚胺树脂粉,其分子结构如下述式(A)所示:A low thermal expansion coefficient soluble polyimide resin powder, the molecular structure of which is shown in the following formula (A):

Figure BDA0002284320420000021
Figure BDA0002284320420000021

其中:in:

式(A)中二胺基团和二酐基团的摩尔比为1:1;The molar ratio of diamine group and dianhydride group in formula (A) is 1:1;

Ar1表示下述式(Ar1-1)至式(Ar1-8)以及它们的异构体中的任意一种:Ar1 represents any one of the following formulae (Ar1-1) to (Ar1-8) and their isomers:

Figure BDA0002284320420000022
Figure BDA0002284320420000022

Ar2表示下述式(Ar2-1)至式(Ar2-10)以及它们的异构体中的任意一种:Ar2 represents any one of the following formulae (Ar2-1) to (Ar2-10) and their isomers:

Figure BDA0002284320420000023
Figure BDA0002284320420000023

D表示刚性直链嵌段,该嵌段在式(A)所示总分子结构中所占的比例为15~60mol%,该嵌段由下述式(B)所示的重复结构单元构成:D represents a rigid straight chain block, and the proportion of the block in the total molecular structure represented by the formula (A) is 15-60 mol%, and the block is composed of the repeating structural unit represented by the following formula (B):

Figure BDA0002284320420000031
其中,
Figure BDA0002284320420000031
in,

a=2~20;a=2~20;

Ar3表示下述式(Ar3-1)至式(Ar3-5)以及它们的异构体中的任意一种:Ar3 represents any one of the following formulae (Ar3-1) to (Ar3-5) and their isomers:

Figure BDA0002284320420000032
Figure BDA0002284320420000032

本发明所述的低热膨胀系数可溶性聚酰亚胺树脂粉在不加热条件下可溶解于非质子性极性溶剂(如N,N-二甲基甲酰胺、N,N-二甲基乙酰胺、N,N-二乙基乙酰胺、二甲基亚砜、N-甲基-2-吡咯烷酮、1,3-二甲基-2-咪唑烷酮等),在加热条件下可溶解于甲苯、环己酮等溶剂中。本发明所述的低热膨胀系数可溶性聚酰亚胺树脂粉的溶解量在1/l0g以上,包含加热措施。The low thermal expansion coefficient soluble polyimide resin powder of the present invention can be dissolved in aprotic polar solvents (such as N,N-dimethylformamide, N,N-dimethylacetamide) without heating , N,N-diethylacetamide, dimethyl sulfoxide, N-methyl-2-pyrrolidone, 1,3-dimethyl-2-imidazolidinone, etc.), soluble in toluene under heating conditions , cyclohexanone and other solvents. The dissolving amount of the low thermal expansion coefficient soluble polyimide resin powder of the present invention is more than 1/10 g, including heating measures.

本发明还提供上述低热膨胀系数可溶性聚酰亚胺树脂粉的制备方法,包括制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤以及由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤,其中,所述制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤包括:The present invention also provides a method for preparing the above-mentioned low thermal expansion coefficient soluble polyimide resin powder, including the steps of preparing a low thermal expansion coefficient soluble polyamic acid resin solution and preparing the low thermal expansion coefficient soluble polyamic acid resin solution from the low thermal expansion coefficient soluble polyamic acid resin solution. The step of imine resin powder, wherein, the step of preparing low thermal expansion coefficient soluble polyamic acid resin solution comprises:

第一步:使4,4’-二氨基-2,2’-双三氟甲基联苯(TFDB)与主体结构为Ar3所示结构的二酐单体在非质子极性溶剂反应,得到嵌段聚酰胺酸树脂溶液;其中,The first step: react 4,4'-diamino-2,2'-bistrifluoromethyl biphenyl (TFDB) with a dianhydride monomer whose main structure is Ar3 in an aprotic polar solvent to obtain Block polyamic acid resin solution; wherein,

Ar3表示下述式(Ar3-1)至式(Ar3-5)以及它们的异构体中的任意一种:Ar3 represents any one of the following formulae (Ar3-1) to (Ar3-5) and their isomers:

Figure BDA0002284320420000033
Figure BDA0002284320420000033

第二步:向所得嵌段聚酰胺酸树脂溶液中加入主体结构为Ar1所示结构的二胺单体和非质子极性溶剂,之后再分批加入主体结构为Ar2所示结构的二酐单体反应,得到低热膨胀系数可溶性聚酰胺酸树脂溶液;其中,The second step: add the diamine monomer and aprotic polar solvent whose main structure is the structure shown by Ar1 to the obtained block polyamic acid resin solution, and then add the dianhydride monomer whose main structure is the structure shown by Ar2 in batches body reaction to obtain a low thermal expansion coefficient soluble polyamic acid resin solution; wherein,

所述主体结构为Ar1所示结构的二胺单体及主体结构为Ar2所示结构的二酐单体的加入量为控制所得低热膨胀系数可溶性聚酰胺酸树脂中嵌段聚酰胺酸树脂所占的比例为15~60mol%,且所加入的主体结构为Ar2所示结构的二酐单体及主体结构为Ar1所示结构的二胺单体使得在所得低热膨胀系数可溶性聚酰胺酸树脂中二胺基团和二酐基团的摩尔比为1:1;The addition amount of the diamine monomer whose main structure is the structure represented by Ar1 and the dianhydride monomer whose main structure is the structure represented by Ar2 is to control the proportion of the block polyamic acid resin in the obtained low thermal expansion coefficient soluble polyamic acid resin. The ratio is 15-60 mol%, and the added dianhydride monomer with the main structure of Ar2 and the diamine monomer with the main structure of Ar1 makes the obtained low thermal expansion coefficient soluble polyamic acid resin. The molar ratio of amine groups and dianhydride groups is 1:1;

Ar1表示下述式(Ar1-1)至式(Ar1-8)以及它们的异构体中的任意一种:Ar1 represents any one of the following formulae (Ar1-1) to (Ar1-8) and their isomers:

Figure BDA0002284320420000041
Figure BDA0002284320420000041

Ar2表示下述式(Ar2-1)至式(Ar2-10)以及它们的异构体中的任意一种:Ar2 represents any one of the following formulae (Ar2-1) to (Ar2-10) and their isomers:

Figure BDA0002284320420000042
Figure BDA0002284320420000042

本发明通过在聚酰亚胺分子结构中引入氟侧基降低分子间的共轭效应,增加聚酰亚胺分子链的间距,同时减小分子链间的作用力,破坏分子链的紧密堆砌,使其自由体积变大,有利于溶剂分子进入聚酰亚胺树脂体系使其溶胀直至溶解,从而提高所得聚酰亚胺树脂的溶剂可溶性;而引入由刚性芳香族二酐单体和具有吸电子性较强的氟侧基二胺构成的刚性直链嵌段,并控制嵌段重复结构单元数及嵌段所占比例,使所得可溶性聚酰亚胺树脂保持较低的热膨胀系数。The invention reduces the conjugation effect between molecules by introducing fluorine side groups into the molecular structure of polyimide, increases the spacing of polyimide molecular chains, reduces the force between molecular chains, and destroys the tight stacking of molecular chains. Make its free volume larger, which is beneficial for solvent molecules to enter the polyimide resin system to swell until dissolved, thereby improving the solvent solubility of the obtained polyimide resin; while the introduction of rigid aromatic dianhydride monomers and electron-withdrawing monomers The rigid straight-chain block composed of the fluorine pendant diamine with strong property is controlled, and the number of repeating structural units of the block and the proportion of the block are controlled, so that the obtained soluble polyimide resin maintains a low thermal expansion coefficient.

上述制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤的第一步中,非质子极性溶剂的用量通常为控制所得嵌段聚酰胺酸树脂溶液中嵌段聚酰胺酸树脂的固含量为10~25%,优选为10~15%;体系中TFDB相对于主体结构为Ar3所示结构的二酐单体过量,所述主体结构为Ar3所示结构的二酐单体具体可以是选自均苯四酸二酐(PMDA)、3,3',4,4'-联苯四羧酸二酐和2,3,3'4'-联苯四甲酸二酐、二苯酮四羧酸二酐(BTDA)、1,4,5,8-萘四甲酸酐(NTCDA)、环己烷四酸二酐(HPMDA)中的任意一种。该步骤中,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数优选为2~20。In the first step of the above step of preparing the low thermal expansion coefficient soluble polyamic acid resin solution, the amount of the aprotic polar solvent is usually controlled to control the solid content of the block polyamic acid resin in the obtained block polyamic acid resin solution to be 10~ 25%, preferably 10-15%; TFDB in the system is in excess relative to the dianhydride monomer whose main structure is the structure represented by Ar3, and the dianhydride monomer whose main structure is the structure represented by Ar3 can be selected from homobenzene. Tetracarboxylic dianhydride (PMDA), 3,3',4,4'-biphenyltetracarboxylic dianhydride and 2,3,3'4'-biphenyltetracarboxylic dianhydride, benzophenone tetracarboxylic dianhydride (BTDA), any one of 1,4,5,8-naphthalenetetracarboxylic anhydride (NTCDA) and cyclohexanetetracarboxylic dianhydride (HPMDA). In this step, the number of repeating structural units in the obtained block polyamic acid resin solution is preferably 2-20.

上述制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤的第二步中,非质子极性溶剂的用量通常为控制所得低热膨胀系数可溶性聚酰胺酸树脂溶液中低热膨胀系数可溶性聚酰胺酸树脂的固含量为10~25%,优选为10~15%;所述主体结构为Ar1所示结构的二胺单体具体可以是选自3,4-二氨基二苯醚(3,4-ODA)、3,3’二氨基二苯基醚(3,3-ODA)、4,4-二氨基二苯醚(4,4-ODA)、2,2-二[4-(4-氨基苯氧基)苯基]丙烷(BAPP)、全间位三苯二醚二胺、1,3-双(4-氨基苯氧基)苯(TPER)、3,5二氨基4′苯炔基二苯甲酮、N,N'-二苯基联苯二胺、3,3'-二氨基二苯甲酮、4,4’-二氨基二苯基二氟甲烷、2,2-二(4-氨基苯)-丙烷、双(4-(3-氨基苯氧基)苯基)硫醚(BAS)、4,4’-二氨基二苯基硫醚、3,4’-二氨基二苯基硫醚和双(4-(3-氨基苯氧基)苯基)砜、1,6-己二胺、1,9-壬二胺和1,10-二氨基癸烷中的任意一种;所述主体结构为Ar2所示结构的二酐单体具体中以是选自3,3',4,4'-联苯四羧酸二酐(s-BPDA)、2,3,3'4'-联苯四甲酸二酐(a-BPDA)、3,3',4,4'-二苯基砜四羧酸二酸酐(OBDP)、丁烷四羧酸二酐、环己烷四酸二酐、3,3',4,4'-二苯醚四甲酸二酐(ODPA)、4,4-六氟异丙基邻苯二甲酸酐(6FDA)、二苯酮四羧酸二酐(BTDA)、双酚A型二醚二酐(BPADA)和三苯双醚二酐中的任意一种。In the second step of the above step of preparing the low thermal expansion coefficient soluble polyamic acid resin solution, the amount of the aprotic polar solvent is usually controlled to control the solidity of the low thermal expansion coefficient soluble polyamic acid resin in the obtained low thermal expansion coefficient soluble polyamic acid resin solution. The content is 10-25%, preferably 10-15%; the diamine monomer whose main structure is the structure represented by Ar1 can be specifically selected from 3,4-diaminodiphenyl ether (3,4-ODA), 3,3'diaminodiphenyl ether (3,3-ODA), 4,4-diaminodiphenyl ether (4,4-ODA), 2,2-bis[4-(4-aminophenoxy) ) phenyl] propane (BAPP), all-meta-triphenylenediether diamine, 1,3-bis(4-aminophenoxy)benzene (TPER), 3,5-diamino4'benzynyldiphenylmethane Ketone, N,N'-diphenylbenzidine, 3,3'-diaminobenzophenone, 4,4'-diaminodiphenyldifluoromethane, 2,2-bis(4-amino Benzene)-propane, bis(4-(3-aminophenoxy)phenyl)sulfide (BAS), 4,4'-diaminodiphenyl sulfide, 3,4'-diaminodiphenyl sulfide Ether and any one of bis(4-(3-aminophenoxy)phenyl)sulfone, 1,6-hexanediamine, 1,9-nonanediamine and 1,10-diaminodecane; all The dianhydride monomer whose main structure is the structure represented by Ar2 is specifically selected from 3,3',4,4'-biphenyltetracarboxylic dianhydride (s-BPDA), 2,3,3'4' -Biphenyltetracarboxylic dianhydride (a-BPDA), 3,3',4,4'-diphenylsulfone tetracarboxylic dianhydride (OBDP), butane tetracarboxylic dianhydride, cyclohexane tetracarboxylic dianhydride anhydride, 3,3',4,4'-diphenyl ether tetracarboxylic dianhydride (ODPA), 4,4-hexafluoroisopropyl phthalic anhydride (6FDA), benzophenone tetracarboxylic dianhydride ( Any one of BTDA), bisphenol A type diether dianhydride (BPADA) and triphenyl bisether dianhydride.

上述制备方法中所述的由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤为:将低热膨胀系数可溶性聚酰胺酸树脂溶液以化学亚胺化方式或热亚胺化方式进行亚胺化,得到低热膨胀系数可溶性聚酰亚胺树脂粉;其中亚胺化在≤250℃条件下进行。更为优选的,在≤200℃条件下即可亚胺化完全。具体的:The step of preparing the low thermal expansion coefficient soluble polyimide resin powder from the low thermal expansion coefficient soluble polyamic acid resin solution described in the above preparation method is: chemically imidizing the low thermal expansion coefficient soluble polyamic acid resin solution or thermally. The imidization method is carried out to obtain a low thermal expansion coefficient soluble polyimide resin powder; wherein the imidization is carried out under the condition of ≤250°C. More preferably, the imidization can be completed under the condition of ≤200°C. specific:

当以化学亚胺化方式进行亚胺化时,所述由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤为:将低热膨胀系数可溶性聚酰胺酸树脂溶液置于反应容器中,向其中滴加胺类催化剂、脱水剂和二甲苯,控制所得体系中低热膨胀系数可溶性聚酰胺酸树脂固含量为5~10%,之后于加热或不加热条件下反应,反应完成后,冷却,将反应物料转入劣溶剂中,过滤,洗涤,滤饼在真空且温度≤250℃条件下亚胺化,得到低热膨胀系数可溶性聚酰亚胺树脂粉。When the imidization is carried out by chemical imidization, the step of preparing the low thermal expansion coefficient soluble polyimide resin powder from the low thermal expansion coefficient soluble polyamic acid resin solution is as follows: Put it in a reaction vessel, drop amine catalyst, dehydrating agent and xylene into it, control the solid content of the low thermal expansion coefficient soluble polyamic acid resin in the obtained system to be 5-10%, and then react under heating or non-heating conditions, After the reaction is completed, cool, transfer the reaction material into a poor solvent, filter, wash, and imidize the filter cake under the condition of vacuum and temperature≤250℃ to obtain low thermal expansion coefficient soluble polyimide resin powder.

采用上述化学亚胺化时,反应通常在30~150℃条件下进行,反应时间优选为1~12h;当亚胺化温度为200℃时,时间优选控制在10~12h。其中涉及的胺类催化剂和脱水剂及它们的加入量均为现有技术中的常规选择,优选的,胺类催化剂可以是三乙胺、吡啶、二甲基吡啶和异喹啉中的任意一种或两种组合;脱水剂可以是乙酸酐和/或丙酸酐。其中二酐:催化剂:脱水剂摩尔当量比为1:1:1.5,而脱水剂的加入量通常为催化剂摩尔量的1~2倍,优选为1.5倍。When the above chemical imidization is adopted, the reaction is usually carried out at 30-150 °C, and the reaction time is preferably 1-12 h; when the imidization temperature is 200 °C, the time is preferably controlled at 10-12 h. The amine catalyst and dehydrating agent involved and their additions are conventional selections in the prior art, preferably, the amine catalyst can be any one of triethylamine, pyridine, lutidine and isoquinoline one or a combination of two; the dehydrating agent can be acetic anhydride and/or propionic anhydride. The molar equivalent ratio of dianhydride:catalyst:dehydrating agent is 1:1:1.5, and the amount of dehydrating agent added is usually 1-2 times the molar amount of the catalyst, preferably 1.5 times.

当以热亚胺化方式进行亚胺化时,所述由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤为:将低热膨胀系数可溶性聚酰胺酸树脂溶液置于反应容器中,向其中加入二甲苯,控制所得体系中低热膨胀系数可溶性聚酰胺酸树脂固含量为5~10%,之后于加热条件下反应,反应完成后,冷却,将反应物料转入劣溶剂中,洗涤,过滤,滤饼在真空且温度≤250℃条件下亚胺化,得到低热膨胀系数可溶性聚酰亚胺树脂粉。When the imidization is carried out by thermal imidization, the step of preparing the low thermal expansion coefficient soluble polyimide resin powder from the low thermal expansion coefficient soluble polyamic acid resin solution is as follows: Place in the reaction vessel, add xylene to it, control the solid content of the low thermal expansion coefficient soluble polyamic acid resin in the obtained system to be 5-10%, then react under heating conditions, after the reaction is completed, cool, and transfer the reaction material into In a poor solvent, wash, filter, and imidize the filter cake under the conditions of vacuum and temperature ≤ 250 ℃ to obtain low thermal expansion coefficient soluble polyimide resin powder.

采用上述热亚胺化时,反应通常在溶剂的回流温度下进行,反应时间通常为1~12h;当亚胺化温度为200℃时,时间优选控制在10~12h。上述两种亚胺化方法中涉及的劣溶剂与现有技术相同,具体可以是选自丙酮、甲醇和乙醇中的任意一种或两种以上的组合。When the above thermal imidization is adopted, the reaction is usually carried out at the reflux temperature of the solvent, and the reaction time is usually 1-12 h; when the imidization temperature is 200° C., the time is preferably controlled at 10-12 h. The inferior solvents involved in the above two imidization methods are the same as those in the prior art, and can specifically be any one or a combination of two or more selected from acetone, methanol and ethanol.

本发明所述方法中涉及的非质子极性溶剂与现有技术相同,具体可以是选自N,N-二甲基甲酰胺、N,N-二甲基乙酰胺、二甲基亚砜、N-甲基吡咯烷酮和γ-丁内酯等中的任意一种或两种组合。The aprotic polar solvent involved in the method of the present invention is the same as the prior art, and can be specifically selected from N,N-dimethylformamide, N,N-dimethylacetamide, dimethyl sulfoxide, Any one or a combination of N-methylpyrrolidone and γ-butyrolactone, etc.

本发明还包括由上述方法制备得到的低热膨胀系数可溶性聚酰亚胺树脂粉。The present invention also includes the low thermal expansion coefficient soluble polyimide resin powder prepared by the above method.

本发明所述的低热膨胀系数可溶性聚酰亚胺树脂粉可溶于非质子极性溶剂中进一步制备成聚酰亚胺胶、聚酰亚胺薄膜或聚酰亚胺清漆,经热处理得到高性能薄膜材料或绝缘漆膜。所得薄膜可适用于半导体芯片的钝化保护膜、电子器件的缓冲内涂膜、焊接点保护膜以及多层金属互连结构的层间绝缘膜。The low thermal expansion coefficient soluble polyimide resin powder of the present invention can be dissolved in aprotic polar solvents to be further prepared into polyimide glue, polyimide film or polyimide varnish, and heat treatment to obtain high performance Thin film material or insulating paint film. The obtained thin film can be applied to the passivation protective film of semiconductor chips, the buffer inner coating film of electronic devices, the protective film of solder joints and the interlayer insulating film of the multi-layer metal interconnection structure.

具体的,将本发明所述低热膨胀系数可溶性聚酰亚胺树脂粉制备成低热膨胀系数可溶性聚酰亚胺薄膜的方法如下:将所得低热膨胀系数可溶性聚酰亚胺树脂粉溶解于非质子极性溶剂中,得到具有一定粘度的树脂溶液,脱泡后涂布在光洁玻璃板上,按照从低温到高温的程序进行亚胺化(如按80℃/1h+130℃/0.5h+180℃/0.5h+200℃/0.5h的程度亚胺化),即可得到低热膨胀系数可溶性聚酰亚胺薄膜。Specifically, the method for preparing the low thermal expansion coefficient soluble polyimide resin powder of the present invention into a low thermal expansion coefficient soluble polyimide film is as follows: dissolving the obtained low thermal expansion coefficient soluble polyimide resin powder in an aprotic electrode A resin solution with a certain viscosity is obtained in a neutral solvent, which is coated on a clear glass plate after defoaming, and imidized according to the procedure from low temperature to high temperature (such as 80°C/1h+130°C/0.5h+180°C). /0.5h+200℃/0.5h degree of imidization), the low thermal expansion coefficient soluble polyimide film can be obtained.

与现有技术相比,本发明的特点在于:Compared with the prior art, the characteristics of the present invention are:

1、通过在聚酰亚胺分子结构中引入氟侧基降低分子间的共轭效应,增加聚合物分子链的间距,同时减小分子链间的作用力,破坏分子链的紧密堆砌,使其自由体积变大,有利于溶剂分子进入聚酰亚胺树脂体系使其溶胀直至溶解,从而提高所得聚酰亚胺树脂的溶剂可溶性;而引入由刚性芳香族二酐单体和具有吸电子性较强的氟侧基二胺构成的刚性直链嵌段,并控制嵌段重复结构单元数及嵌段所占比例,使所得可溶性聚酰亚胺树脂保持良好的热膨胀系数;此外,从刚性链段与柔性链段的兼容性问题出发,利用不同聚合物之间的互补性和协同性,通过将刚性嵌段聚合物与柔性嵌段聚合物共聚,实现在不形成大量结晶物的同时改善可溶性聚酰亚胺树脂的加工性。因此,采用本发明所述方法制得的聚酰亚胺树脂粉可溶解于DMAc、NMP、甲苯和环己酮等极性溶剂,且具有较低的热膨胀系数,接近金属铜箔,在电子元器件上具有更有价值的应用前景。1. By introducing fluorine side groups into the molecular structure of polyimide, the conjugation effect between molecules is reduced, the distance between polymer molecular chains is increased, the force between molecular chains is reduced, and the close stacking of molecular chains is destroyed, so that the The free volume becomes larger, which is beneficial for the solvent molecules to enter the polyimide resin system and swell until dissolved, thereby improving the solvent solubility of the obtained polyimide resin; while the introduction of rigid aromatic dianhydride monomers and relatively electron-absorbing properties The rigid straight-chain block composed of strong fluorine pendant diamine, and the number of repeating structural units and the proportion of the block are controlled, so that the obtained soluble polyimide resin maintains a good thermal expansion coefficient; in addition, from the rigid segment Starting from the compatibility problem with the flexible segment, by utilizing the complementarity and synergy between different polymers, by copolymerizing the rigid block polymer with the flexible block polymer, it is possible to improve the soluble polymer without forming a large number of crystals. Processability of imide resins. Therefore, the polyimide resin powder prepared by the method of the present invention can be dissolved in polar solvents such as DMAc, NMP, toluene and cyclohexanone, and has a low thermal expansion coefficient, which is close to that of metal copper foil. The device has more valuable application prospects.

2、采用本发明所述低热膨胀系数可溶性聚酰亚胺树脂粉按常规方法制成的聚酰亚胺薄膜具有较低的热膨胀系数,可低至16.1ppm/K。2. The polyimide film prepared by using the low thermal expansion coefficient soluble polyimide resin powder of the present invention according to the conventional method has a low thermal expansion coefficient, which can be as low as 16.1ppm/K.

具体实施方式Detailed ways

下面结合具体实施例对本发明作进一步的详述,以更好地理解本发明的内容,但本发明并不限于以下实施例。The present invention will be described in further detail below in conjunction with specific embodiments to better understand the content of the present invention, but the present invention is not limited to the following embodiments.

以下各实施例中所述的份数为重量份。The parts described in the following examples are parts by weight.

实施例1Example 1

具体制备方法为:The specific preparation method is:

1)制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤:1) The steps of preparing the low thermal expansion coefficient soluble polyamic acid resin solution:

第一步:取27.293份的TFDB和250份非质子极性溶剂N,N-二甲基甲酰胺置于带有电动搅拌器的三口烧瓶中,搅拌至完全溶解,加入12.394份PMDA单体,搅拌反应2h,得到嵌段聚酰胺酸树脂溶液,备用;其中,体系中TFDB相对于PMDA单体过量,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数为2;The first step: take 27.293 parts of TFDB and 250 parts of aprotic polar solvent N,N-dimethylformamide and put them in a three-necked flask with an electric stirrer, stir until completely dissolved, add 12.394 parts of PMDA monomer, The reaction was stirred for 2h to obtain a block polyamic acid resin solution for subsequent use; wherein, in the system, TFDB was excessive relative to the PMDA monomer, and the number of repeating structural units in the obtained block polyamic acid resin solution was 2;

第二步:向所得嵌段聚酰胺酸树脂溶液中加入39.81份3,4-ODA和600份非质子极性溶剂N,N-二甲基甲酰胺,搅拌至单体完全溶解,然后加入70.503份ODPA单体(分3次加入),搅拌反应4h,得到低热膨胀系数可溶性聚酰胺酸树脂溶液,粘度为0.8万mpa·s;整个体系中二胺单体和二酐单体的摩尔比为1:1,嵌段聚酰胺酸树脂在体系中所占的比例为20mol%,固体含量15%;The second step: add 39.81 parts of 3,4-ODA and 600 parts of aprotic polar solvent N,N-dimethylformamide to the obtained block polyamic acid resin solution, stir until the monomer is completely dissolved, and then add 70.503 ODPA monomer (added in 3 times), stirred and reacted for 4 hours to obtain a low thermal expansion coefficient soluble polyamic acid resin solution with a viscosity of 08,000 mpa·s; the molar ratio of diamine monomer and dianhydride monomer in the whole system was 1:1, the proportion of block polyamic acid resin in the system is 20mol%, and the solid content is 15%;

2)由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤:2) The steps of preparing low thermal expansion coefficient soluble polyimide resin powder from low thermal expansion coefficient soluble polyamic acid resin solution:

将所得低热膨胀系数可溶性聚酰胺酸树脂溶液置于三口烧瓶中,之后装配滴液漏斗,在搅拌的状态下,缓慢滴加22.95份吡啶、44.43份乙酸酐以及500份二甲苯的混合液体,待滴完后移去滴液漏斗,所得体系中低热膨胀系数可溶性聚酰胺酸树脂固含量为10%;然后将三口烧瓶置于加热套上,缓慢升温到150℃下并保温反应1h,之后冷却到室温;将反应物料缓慢倒入乙醇中,搅拌、减压过滤,用水洗涤2次,之后在真空条件下200℃/12h亚胺化完全,即得到低热膨胀系数可溶性聚酰亚胺树脂粉。所得树脂粉在有机溶剂中的溶解性如表1所示。The obtained low thermal expansion coefficient soluble polyamic acid resin solution was placed in a three-necked flask, then a dropping funnel was assembled, and under stirring, the mixed liquid of 22.95 parts of pyridine, 44.43 parts of acetic anhydride and 500 parts of xylene was slowly added dropwise. After the dropping, the dropping funnel was removed, and the solid content of the low thermal expansion coefficient soluble polyamic acid resin in the obtained system was 10%; then the three-necked flask was placed on the heating mantle, and the temperature was slowly raised to 150 ° C and kept for 1 h, and then cooled to room temperature; slowly pour the reaction material into ethanol, stir, filter under reduced pressure, wash twice with water, and then complete imidization under vacuum at 200°C/12h to obtain low thermal expansion coefficient soluble polyimide resin powder. The solubility of the obtained resin powder in the organic solvent is shown in Table 1.

取10份本实施例所得低热膨胀系数可溶性聚酰亚胺树脂粉溶解于90份N,N-二甲基甲酰胺中,脱泡后得到透明均匀的树脂溶液,然后将其涂覆在光洁的平板上,置于鼓风干燥箱中,按照80℃/1h+130℃/0.5h+180℃/0.5h+200℃/0.5h的程序进行亚胺化,即得到低热膨胀系数可溶性聚酰亚胺薄膜。检测所得薄膜的热膨胀系数CTE结果如表1所示。Take 10 parts of the low thermal expansion coefficient soluble polyimide resin powder obtained in this example and dissolve it in 90 parts of N,N-dimethylformamide to obtain a transparent and uniform resin solution after defoaming, and then coat it on a smooth Place it on a flat plate, place it in a blast drying oven, and carry out imidization according to the procedure of 80°C/1h+130°C/0.5h+180°C/0.5h+200°C/0.5h to obtain a low thermal expansion coefficient soluble polyimide Amine film. The thermal expansion coefficient CTE results of the obtained films are shown in Table 1.

实施例2Example 2

具体制备方法为:The specific preparation method is:

1)制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤:1) The steps of preparing the low thermal expansion coefficient soluble polyamic acid resin solution:

第一步:取59.901份的TFDB和250份非质子极性溶剂DMAc置于带有电动搅拌器的三口烧瓶中,搅拌至完全溶解,加入34.0份PMDA单体,搅拌反应2h,得到嵌段聚酰胺酸树脂溶液,备用;其中,体系中TFDB相对于PMDA单体过量,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数为5;The first step: take 59.901 parts of TFDB and 250 parts of aprotic polar solvent DMAc and place them in a three-necked flask with an electric stirrer, stir until completely dissolved, add 34.0 parts of PMDA monomer, and stir for 2h to obtain a block polymer. The amic acid resin solution is for subsequent use; wherein, in the system, TFDB is excessive relative to the PMDA monomer, and the number of repeating structural units in the obtained block polyamic acid resin solution is 5;

第二步:向所得嵌段聚酰胺酸树脂溶液中加入24.963份3,4-ODA和550份非质子极性溶剂DMAc,搅拌至单体完全溶解,然后加入81.135份BPADA单体(分3次加入),搅拌反应4h,得到低热膨胀系数可溶性聚酰胺酸树脂溶液,粘度为1.2万mpa·s;整个体系中二胺单体和二酐单体的摩尔比为1:1,嵌段聚酰胺酸树脂在体系中所占的比例为50mol%,固体含量为20%;The second step: add 24.963 parts of 3,4-ODA and 550 parts of aprotic polar solvent DMAc to the obtained block polyamic acid resin solution, stir until the monomer is completely dissolved, then add 81.135 parts of BPADA monomer (divided into 3 times) Add), stirring and reacting for 4 hours to obtain a low thermal expansion coefficient soluble polyamic acid resin solution with a viscosity of 12,000 mpa s; the molar ratio of diamine monomer and dianhydride monomer in the whole system is 1:1, and the block polyamide The proportion of acid resin in the system is 50mol%, and the solid content is 20%;

2)由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤:2) The steps of preparing low thermal expansion coefficient soluble polyimide resin powder from low thermal expansion coefficient soluble polyamic acid resin solution:

将所得低热膨胀系数可溶性聚酰胺酸树脂溶液置于三口烧瓶中,之后装配滴液漏斗,在搅拌的状态下,缓慢滴加20.114份二甲基吡啶、33.12份乙酸酐以及250份二甲苯的混合液体,待滴完后移去滴液漏斗,所得体系中低热膨胀系数可溶性聚酰胺酸树脂固含量为16%;然后将三口烧瓶置于加热套上,缓慢升温到30℃下并保温反应12h,之后冷却到室温;将反应物料缓慢倒入乙醇中,搅拌、减压过滤,用水洗涤2次,之后在真空条件下200℃/12h亚胺化完全,即得到低热膨胀系数可溶性聚酰亚胺树脂粉。所得树脂粉在有机溶剂中的溶解性如表1所示。The obtained low thermal expansion coefficient soluble polyamic acid resin solution was placed in a three-necked flask, then a dropping funnel was assembled, and under stirring, a mixture of 20.114 parts of lutidine, 33.12 parts of acetic anhydride and 250 parts of xylene was slowly added dropwise. After dropping the liquid, remove the dropping funnel, and the solid content of the low thermal expansion coefficient soluble polyamic acid resin in the obtained system is 16%; then place the three-necked flask on the heating mantle, slowly heat up to 30 ° C and keep the reaction for 12 h, Then cooled to room temperature; slowly poured the reaction material into ethanol, stirred, filtered under reduced pressure, washed twice with water, and then completely imidized under vacuum at 200°C/12h to obtain a low thermal expansion coefficient soluble polyimide resin pink. The solubility of the obtained resin powder in the organic solvent is shown in Table 1.

取10份本实施例所得低热膨胀系数可溶性聚酰亚胺树脂粉溶解于90份DMAc中,脱泡后得到透明均匀的树脂溶液,然后将其涂覆在光洁的平板上,置于鼓风干燥箱中,按照80℃/1h+130℃/0.5h+180℃/0.5h+200℃/0.5h的程序进行亚胺化,即得到低热膨胀系数可溶性聚酰亚胺薄膜。检测所得薄膜的热膨胀系数CTE,结果如表1所示。Take 10 parts of the low thermal expansion coefficient soluble polyimide resin powder obtained in this example and dissolve it in 90 parts of DMAc. After defoaming, a transparent and uniform resin solution is obtained, which is then coated on a smooth flat plate and placed in blast drying. In the box, the imidization was carried out according to the procedure of 80°C/1h+130°C/0.5h+180°C/0.5h+200°C/0.5h to obtain a low thermal expansion coefficient soluble polyimide film. The thermal expansion coefficient CTE of the obtained film was tested, and the results are shown in Table 1.

实施例3Example 3

具体制备方法为:The specific preparation method is:

1)制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤:1) The steps of preparing the low thermal expansion coefficient soluble polyamic acid resin solution:

第一步:取13.702份TFDB和250份非质子极性溶剂NMP置于带有电动搅拌器的三口烧瓶中,搅拌至完全溶解,加入8.711份PMDA单体,搅拌反应2h,得到嵌段聚酰胺酸树脂溶液,备用;其中,体系中TFDB相对于PMDA单体过量,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数为12;The first step: take 13.702 parts of TFDB and 250 parts of aprotic polar solvent NMP and place them in a three-necked flask with an electric stirrer, stir until completely dissolved, add 8.711 parts of PMDA monomer, and stir for 2 hours to obtain a block polyamide Acid resin solution, standby; Wherein, in the system, TFDB is excessive relative to PMDA monomer, and the number of repeating structural units in the gained block polyamic acid resin solution is 12;

第二步:向所得嵌段聚酰胺酸树脂溶液中加入48.538份3,4-ODA和600份非质子极性溶剂NMP,搅拌至单体完全溶解,然后加入79.049份BTDA单体(分3次加入),搅拌反应4h,得到低热膨胀系数可溶性聚酰胺酸树脂溶液,粘度为1.2万mpa·s;整个体系中二胺单体和二酐单体的摩尔比为1:1,嵌段聚酰胺酸树脂在体系中所占的比例为14mol%,固体含量15%;The second step: add 48.538 parts of 3,4-ODA and 600 parts of aprotic polar solvent NMP to the obtained block polyamic acid resin solution, stir until the monomer is completely dissolved, and then add 79.049 parts of BTDA monomer (in 3 times Add), stirring and reacting for 4 hours to obtain a low thermal expansion coefficient soluble polyamic acid resin solution with a viscosity of 12,000 mpa s; the molar ratio of diamine monomer and dianhydride monomer in the whole system is 1:1, and the block polyamide The proportion of acid resin in the system is 14mol%, and the solid content is 15%;

2)由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤:2) The steps of preparing low thermal expansion coefficient soluble polyimide resin powder from low thermal expansion coefficient soluble polyamic acid resin solution:

将所得低热膨胀系数可溶性聚酰胺酸树脂溶液置于三口烧瓶中,之后装配滴液漏斗,在搅拌的状态下,缓慢滴加40.565份三乙胺、61.388份乙酸酐以及875份二甲苯的混合液体,待滴完后移去滴液漏斗,所得体系中低热膨胀系数可溶性聚酰胺酸树脂固含量为8%;然后将三口烧瓶置于加热套上,缓慢升温到120℃下并保温反应2h,之后冷却到室温;将反应物料缓慢倒入乙醇中,搅拌、减压过滤,用水洗涤2次,之后在真空条件下200℃/12h亚胺化完全,即得到低热膨胀系数可溶性聚酰亚胺树脂粉。所得树脂粉在有机溶剂中的溶解性如表1所示。The obtained low thermal expansion coefficient soluble polyamic acid resin solution was placed in a three-necked flask, then a dropping funnel was assembled, and under stirring, the mixed liquid of 40.565 parts of triethylamine, 61.388 parts of acetic anhydride and 875 parts of xylene was slowly added dropwise. , remove the dropping funnel after the dropping, the solid content of the low thermal expansion coefficient soluble polyamic acid resin in the obtained system is 8%; then place the three-necked flask on the heating mantle, slowly heat up to 120 ° C and keep the reaction for 2 h, then Cool to room temperature; slowly pour the reaction material into ethanol, stir, filter under reduced pressure, wash twice with water, and then complete imidization under vacuum at 200°C/12h to obtain low thermal expansion coefficient soluble polyimide resin powder . The solubility of the obtained resin powder in the organic solvent is shown in Table 1.

取10份本实施例所得低热膨胀系数可溶性聚酰亚胺树脂粉溶解于90份NMP中,脱泡后得到透明均匀的树脂溶液,然后将其涂覆在光洁的平板上,置于鼓风干燥箱中,按照80℃/1h+130℃/0.5h+180℃/0.5h+200℃/0.5h的程序进行亚胺化,即得到低热膨胀系数可溶性聚酰亚胺薄膜。对所得薄膜的热膨胀系数等性能进行检测,结果如表1所示。Take 10 parts of the low thermal expansion coefficient soluble polyimide resin powder obtained in this example and dissolve it in 90 parts of NMP to obtain a transparent and uniform resin solution after defoaming, which is then coated on a smooth flat plate and placed in blast drying In the box, the imidization was carried out according to the procedure of 80°C/1h+130°C/0.5h+180°C/0.5h+200°C/0.5h to obtain a low thermal expansion coefficient soluble polyimide film. The thermal expansion coefficient and other properties of the obtained films were tested, and the results are shown in Table 1.

实施例4Example 4

具体制备方法为:The specific preparation method is:

1)制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤:1) The steps of preparing the low thermal expansion coefficient soluble polyamic acid resin solution:

第一步:取23.523份的TFDB和250份非质子极性溶剂N,N-二甲基乙酰胺置于带有电动搅拌器的三口烧瓶中,搅拌至完全溶解,加入16.023份PMDA单体,搅拌反应2h,得到嵌段聚酰胺酸树脂溶液,备用;其中,体系中TFDB相对于PMDA单体过量,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数为20;The first step: take 23.523 parts of TFDB and 250 parts of aprotic polar solvent N,N-dimethylacetamide and put them in a three-necked flask with an electric stirrer, stir until completely dissolved, add 16.023 parts of PMDA monomer, The reaction was stirred for 2h to obtain a block polyamic acid resin solution for subsequent use; wherein, TFDB in the system was excessive relative to the PMDA monomer, and the number of repeating structural units in the obtained block polyamic acid resin solution was 20;

第二步:向所得嵌段聚酰胺酸树脂溶液中加入34.311份3,4-ODA和600份非质子极性溶剂DMAC,搅拌至单体完全溶解,然后加入76.143份6FDA单体(分3次加入),搅拌反应4h,得到低热膨胀系数可溶性聚酰胺酸树脂溶液,粘度为1.5万mpa·s;整个体系中二胺单体和二酐单体的摩尔比为1:1,嵌段聚酰胺酸树脂在体系中所占的比例为30mol%,固体含量15%;The second step: add 34.311 parts of 3,4-ODA and 600 parts of aprotic polar solvent DMAC to the obtained block polyamic acid resin solution, stir until the monomer is completely dissolved, then add 76.143 parts of 6FDA monomer (in 3 times Add), stirring and reacting for 4h to obtain a low thermal expansion coefficient soluble polyamic acid resin solution with a viscosity of 15,000 mpa s; the molar ratio of diamine monomer and dianhydride monomer in the whole system is 1:1, and the block polyamide The proportion of acid resin in the system is 30mol%, and the solid content is 15%;

2)由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤:2) The steps of preparing low thermal expansion coefficient soluble polyimide resin powder from low thermal expansion coefficient soluble polyamic acid resin solution:

将所得低热膨胀系数可溶性聚酰胺酸树脂溶液置于三口烧瓶中,之后装配滴液漏斗,在搅拌的状态下,缓慢滴加19.368份吡啶、37.496份乙酸酐以及500份二甲苯的混合液体,待滴完后移去滴液漏斗,所得体系中低热膨胀系数可溶性聚酰胺酸树脂固含量为10%;然后将三口烧瓶置于加热套上,缓慢升温到80℃下并保温反应10h,之后冷却到室温;将反应物料缓慢倒入乙醇中,搅拌、减压过滤,用水洗涤2次,之后在真空条件下200℃/12h亚胺化完全,即得到低热膨胀系数可溶性聚酰亚胺树脂粉。所得树脂粉在有机溶剂中的溶解性如表1所示。The obtained low thermal expansion coefficient soluble polyamic acid resin solution was placed in a three-necked flask, then a dropping funnel was assembled, and under stirring, the mixed liquid of 19.368 parts of pyridine, 37.496 parts of acetic anhydride and 500 parts of xylene was slowly added dropwise. After the dropping, the dropping funnel was removed, and the solid content of the low thermal expansion coefficient soluble polyamic acid resin in the obtained system was 10%; then the three-necked flask was placed on the heating mantle, slowly heated to 80 ° C and kept for 10 h, and then cooled to room temperature; slowly pour the reaction material into ethanol, stir, filter under reduced pressure, wash twice with water, and then complete imidization under vacuum at 200°C/12h to obtain low thermal expansion coefficient soluble polyimide resin powder. The solubility of the obtained resin powder in the organic solvent is shown in Table 1.

取10份本实施例所得低热膨胀系数可溶性聚酰亚胺树脂粉溶解于90份NMP中,脱泡后得到透明均匀的树脂溶液,然后将其涂覆在光洁的平板上,置于鼓风干燥箱中,按照80℃/1h+130℃/0.5h+180℃/0.5h+200℃/0.5h的程序进行亚胺化,即得到低热膨胀系数可溶性聚酰亚胺薄膜。对所得薄膜的热膨胀系数等性能进行检测,结果如表1所示。Take 10 parts of the low thermal expansion coefficient soluble polyimide resin powder obtained in this example and dissolve it in 90 parts of NMP to obtain a transparent and uniform resin solution after defoaming, which is then coated on a smooth flat plate and placed in blast drying In the box, the imidization was carried out according to the procedure of 80°C/1h+130°C/0.5h+180°C/0.5h+200°C/0.5h to obtain a low thermal expansion coefficient soluble polyimide film. The thermal expansion coefficient and other properties of the obtained films were tested, and the results are shown in Table 1.

实施例5Example 5

具体制备方法为:The specific preparation method is:

1)制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤:1) The steps of preparing the low thermal expansion coefficient soluble polyamic acid resin solution:

第一步:取35.891份的TFDB和250份非质子极性溶剂DMAc置于带有电动搅拌器的三口烧瓶中,搅拌至完全溶解,加入26.38份BPDA单体,搅拌反应2h,得到嵌段聚酰胺酸树脂溶液,备用;其中,体系中TFDB相对于BPDA单体过量,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数为5;The first step: take 35.891 parts of TFDB and 250 parts of aprotic polar solvent DMAc and place them in a three-necked flask with an electric stirrer, stir until completely dissolved, add 26.38 parts of BPDA monomer, and stir and react for 2h to obtain a block polymer. The amic acid resin solution is for subsequent use; wherein, in the system, TFDB is excessive relative to the BPDA monomer, and the number of repeating structural units in the obtained block polyamic acid resin solution is 5;

第二步:向所得嵌段聚酰胺酸树脂溶液中加入46.0018份BAPP和547份非质子极性溶剂DMAC,搅拌至单体完全溶解,然后加入41.72份ODPA单体(分3次加入),搅拌反应4h,得到低热膨胀系数可溶性聚酰胺酸树脂溶液,粘度为1.0万mpa·s;整个体系中二胺单体和二酐单体的摩尔比为1:1,嵌段聚酰胺酸树脂在体系中所占的比例为50mol%,固含量18.8%;The second step: add 46.0018 parts of BAPP and 547 parts of aprotic polar solvent DMAC to the obtained block polyamic acid resin solution, stir until the monomer is completely dissolved, then add 41.72 parts of ODPA monomer (add in 3 times), stir The reaction was carried out for 4 h to obtain a low thermal expansion coefficient soluble polyamic acid resin solution with a viscosity of 10,000 mpa·s; the molar ratio of diamine monomer and dianhydride monomer in the whole system was 1:1, and the block polyamic acid resin was in the system. The proportion of 50mol%, the solid content of 18.8%;

2)由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤:2) The steps of preparing low thermal expansion coefficient soluble polyimide resin powder from low thermal expansion coefficient soluble polyamic acid resin solution:

将所得低热膨胀系数可溶性聚酰胺酸树脂溶液置于三口烧瓶中,之后装配滴液漏斗,在搅拌的状态下,缓慢滴加28.475份异喹啉、43.037份丙酸酐以及500份二甲苯的混合液体,待滴完后移去滴液漏斗,所得体系中低热膨胀系数可溶性聚酰胺酸树脂固含量为11.5%;然后将三口烧瓶置于加热套上,缓慢升温到120℃下并保温反应3h,之后冷却到室温;将反应物料缓慢倒入乙醇中,搅拌、减压过滤,用水洗涤2次,之后在真空条件下200℃/12h亚胺化完全,即得到低热膨胀系数可溶性聚酰亚胺树脂粉。所得树脂粉在有机溶剂中的溶解性如表1所示。The obtained low thermal expansion coefficient soluble polyamic acid resin solution was placed in a three-necked flask, then a dropping funnel was assembled, and under stirring, the mixed liquid of 28.475 parts of isoquinoline, 43.037 parts of propionic anhydride and 500 parts of xylene was slowly added dropwise. , remove the dropping funnel after the dripping, the solid content of the low thermal expansion coefficient soluble polyamic acid resin in the obtained system is 11.5%; then place the three-necked flask on the heating mantle, slowly heat up to 120 ° C and keep the reaction for 3 hours, then Cool to room temperature; slowly pour the reaction material into ethanol, stir, filter under reduced pressure, wash twice with water, and then complete imidization under vacuum at 200°C/12h to obtain low thermal expansion coefficient soluble polyimide resin powder . The solubility of the obtained resin powder in the organic solvent is shown in Table 1.

取10份本实施例所得低热膨胀系数可溶性聚酰亚胺树脂粉溶解于90份NMP中,脱泡后得到透明均匀的树脂溶液,然后将其涂覆在光洁的平板上,置于鼓风干燥箱中,按照80℃/1h+130℃/0.5h+180℃/0.5h+200℃/0.5h的程序进行亚胺化,即得到低热膨胀系数可溶性聚酰亚胺薄膜。对所得薄膜的热膨胀系数等性能进行检测,结果如表1所示。Take 10 parts of the low thermal expansion coefficient soluble polyimide resin powder obtained in this example and dissolve it in 90 parts of NMP to obtain a transparent and uniform resin solution after defoaming, which is then coated on a smooth flat plate and placed in blast drying In the box, the imidization was carried out according to the procedure of 80°C/1h+130°C/0.5h+180°C/0.5h+200°C/0.5h to obtain a low thermal expansion coefficient soluble polyimide film. The thermal expansion coefficient and other properties of the obtained films were tested, and the results are shown in Table 1.

实施例6Example 6

具体制备方法为:The specific preparation method is:

1)制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤:1) The steps of preparing the low thermal expansion coefficient soluble polyamic acid resin solution:

第一步:取35.508份的TFDB和250份非质子极性溶剂DMAc置于带有电动搅拌器的三口烧瓶中,搅拌至完全溶解,加入26.099份BPDA单体,搅拌反应2h,得到嵌段聚酰胺酸树脂溶液,粘度为2.1万mpa·s,备用;其中,体系中TFDB相对于BPDA单体过量,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数为5;The first step: take 35.508 parts of TFDB and 250 parts of aprotic polar solvent DMAc and place them in a three-necked flask with an electric stirrer, stir until completely dissolved, add 26.099 parts of BPDA monomer, and stir for 2h to obtain a block polymer. The amic acid resin solution, with a viscosity of 21,000 mPa·s, is ready for use; wherein, the TFDB in the system is excessive relative to the BPDA monomer, and the number of repeating structural units in the obtained block polyamic acid resin solution is 5;

第二步:向所得嵌段聚酰胺酸树脂溶液中加入45.518份BAPP和600份非质子极性溶剂DMAc,搅拌至单体完全溶解,然后加入42.875份BTDA单体(分3次加入),搅拌反应4h,得到低热膨胀系数可溶性聚酰胺酸树脂溶液,粘度为1.2万mpa·s;整个体系中二胺单体和二酐单体的摩尔比为1:1,嵌段聚酰胺酸树脂在体系中所占的比例为50mol%,固体含量15%;The second step: add 45.518 parts of BAPP and 600 parts of aprotic polar solvent DMAc to the obtained block polyamic acid resin solution, stir until the monomer is completely dissolved, then add 42.875 parts of BTDA monomer (add in 3 times), stir After 4 hours of reaction, a low thermal expansion coefficient soluble polyamic acid resin solution was obtained, with a viscosity of 12,000 mpa·s; the molar ratio of diamine monomer and dianhydride monomer in the whole system was 1:1, and the block polyamic acid resin was in the system. The proportion of 50mol%, the solid content of 15%;

2)由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤:2) The steps of preparing low thermal expansion coefficient soluble polyimide resin powder from low thermal expansion coefficient soluble polyamic acid resin solution:

将所得低热膨胀系数可溶性聚酰胺酸树脂溶液置于三口烧瓶中,之后装配滴液漏斗,再加入500份二甲苯,加热回流状态下反应12h,冷却到室温;将反应物料缓慢倒入乙醇中,搅拌、减压过滤,用丙酮洗涤5次,之后在真空条件下200℃/12h亚胺化完全,即得到低热膨胀系数可溶性聚酰亚胺树脂粉。所得树脂粉在有机溶剂中的溶解性如表1所示。The obtained low thermal expansion coefficient soluble polyamic acid resin solution was placed in a three-necked flask, then a dropping funnel was assembled, 500 parts of xylene were added, and the reaction was conducted under reflux for 12 hours, and then cooled to room temperature; the reaction material was slowly poured into ethanol, Stirring, filtering under reduced pressure, washing with acetone for 5 times, and then complete imidization under vacuum conditions at 200° C./12h to obtain low thermal expansion coefficient soluble polyimide resin powder. The solubility of the obtained resin powder in the organic solvent is shown in Table 1.

将本实施例所得低热膨胀系数可溶性聚酰亚胺树脂粉按实施例5中所述工艺制备低热膨胀系数可溶性聚酰亚胺薄膜。对所得薄膜的热膨胀系数等性能进行检测,结果如表1所示。The low thermal expansion coefficient soluble polyimide resin powder obtained in this example is used to prepare a low thermal expansion coefficient soluble polyimide film according to the process described in Example 5. The thermal expansion coefficient and other properties of the obtained films were tested, and the results are shown in Table 1.

实施例7Example 7

具体制备方法为:The specific preparation method is:

1)制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤:1) The steps of preparing the low thermal expansion coefficient soluble polyamic acid resin solution:

第一步:取32.04份的TFDB和250份非质子极性溶剂DMAc置于带有电动搅拌器的三口烧瓶中,搅拌至完全溶解,加入23.55份BPDA单体,搅拌反应2h,得到嵌段聚酰胺酸树脂溶液,粘度为2.3万mpa·s,备用;其中,体系中TFDB相对于BPDA单体过量,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数为5;The first step: take 32.04 parts of TFDB and 250 parts of aprotic polar solvent DMAc and place them in a three-necked flask with an electric stirrer, stir until completely dissolved, add 23.55 parts of BPDA monomer, and stir for 2h to obtain a block polymer. The amic acid resin solution, with a viscosity of 23,000 mpa s, is ready for use; wherein, the TFDB in the system is excessive relative to the BPDA monomer, and the number of repeating structural units in the obtained block polyamic acid resin solution is 5;

第二步:向所得嵌段聚酰胺酸树脂溶液中加入41.073份BAPP和600份非质子极性溶剂DMAc,搅拌至单体完全溶解,然后加入53.337份6FDA单体(分3次加入),搅拌反应6h,得到低热膨胀系数可溶性聚酰胺酸树脂溶液,粘度为0.8万mpa·s;整个体系中二胺单体和二酐单体的摩尔比为1:1,嵌段聚酰胺酸树脂在体系中所占的比例为50mol%,固体含量15%;The second step: add 41.073 parts of BAPP and 600 parts of aprotic polar solvent DMAc to the obtained block polyamic acid resin solution, stir until the monomer is completely dissolved, then add 53.337 parts of 6FDA monomer (add in 3 times), stir After 6 hours of reaction, a low thermal expansion coefficient soluble polyamic acid resin solution was obtained with a viscosity of 08,000 mpa·s; the molar ratio of diamine monomer and dianhydride monomer in the whole system was 1:1, and the block polyamic acid resin was in the system. The proportion of 50mol%, the solid content of 15%;

2)由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤:2) The steps of preparing low thermal expansion coefficient soluble polyimide resin powder from low thermal expansion coefficient soluble polyamic acid resin solution:

同实施例6。Same as Example 6.

所得低热膨胀系数可溶性聚酰亚胺树脂粉在有机溶剂中的溶解性如表1所示。Table 1 shows the solubility of the obtained low thermal expansion coefficient soluble polyimide resin powder in an organic solvent.

将本实施例所得低热膨胀系数可溶性聚酰亚胺树脂粉按实施例5中所述工艺制备低热膨胀系数可溶性聚酰亚胺薄膜。对所得薄膜的热膨胀系数等性能进行检测,结果如表1所示。The low thermal expansion coefficient soluble polyimide resin powder obtained in this example is used to prepare a low thermal expansion coefficient soluble polyimide film according to the process described in Example 5. The thermal expansion coefficient and other properties of the obtained films were tested, and the results are shown in Table 1.

实施例8Example 8

具体制备方法为:The specific preparation method is:

1)制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤:1) The steps of preparing the low thermal expansion coefficient soluble polyamic acid resin solution:

第一步:取33.874份的TFDB和250份非质子极性溶剂DMAc置于带有电动搅拌器的三口烧瓶中,搅拌至完全溶解,加入26.844份BTDA单体,搅拌反应1h,得到嵌段聚酰胺酸树脂溶液,备用;其中,体系中TFDB相对于BTDA单体过量,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数为5;The first step: take 33.874 parts of TFDB and 250 parts of aprotic polar solvent DMAc and place them in a three-necked flask with an electric stirrer, stir until completely dissolved, add 26.844 parts of BTDA monomer, and stir for 1 h to obtain a block polymer. An amic acid resin solution, for subsequent use; wherein, in the system, TFDB is excessive relative to BTDA monomer, and the number of repeating structural units in the obtained block polyamic acid resin solution is 5;

第二步:向所得嵌段聚酰胺酸树脂溶液中加入45.749份BAS和600份非质子极性溶剂DMAc,搅拌至单体完全溶解,然后加入44.772份OBDP单体(分2次加入),搅拌反应3h,得到低热膨胀系数可溶性聚酰胺酸树脂溶液,粘度为0.6万mpa·s;整个体系中二胺单体和二酐单体的摩尔比为1:1,嵌段聚酰胺酸树脂在体系中所占的比例为50mol%,固体含量15%;The second step: add 45.749 parts of BAS and 600 parts of aprotic polar solvent DMAc to the obtained block polyamic acid resin solution, stir until the monomer is completely dissolved, then add 44.772 parts of OBDP monomer (add in 2 times), stir The reaction was carried out for 3 hours to obtain a low thermal expansion coefficient soluble polyamic acid resin solution with a viscosity of 0.6 million mpa·s; the molar ratio of diamine monomer and dianhydride monomer in the whole system was 1:1, and the block polyamic acid resin was in the system. The proportion of 50mol%, the solid content of 15%;

2)由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤:2) The steps of preparing low thermal expansion coefficient soluble polyimide resin powder from low thermal expansion coefficient soluble polyamic acid resin solution:

同实施例6。Same as Example 6.

所得低热膨胀系数可溶性聚酰亚胺树脂粉在有机溶剂中的溶解性如表1所示。Table 1 shows the solubility of the obtained low thermal expansion coefficient soluble polyimide resin powder in an organic solvent.

将本实施例所得低热膨胀系数可溶性聚酰亚胺树脂粉按实施例5中所述工艺制备低热膨胀系数可溶性聚酰亚胺薄膜。对所得薄膜的热膨胀系数等性能进行检测,结果如表1所示。The low thermal expansion coefficient soluble polyimide resin powder obtained in this example is used to prepare a low thermal expansion coefficient soluble polyimide film according to the process described in Example 5. The thermal expansion coefficient and other properties of the obtained films were tested, and the results are shown in Table 1.

实施例9Example 9

具体制备方法为:The specific preparation method is:

1)制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤:1) The steps of preparing the low thermal expansion coefficient soluble polyamic acid resin solution:

第一步:取32.621份的TFDB和250份非质子极性溶剂DMAc置于带有电动搅拌器的三口烧瓶中,搅拌至完全溶解,加入25.865份BTDA单体,搅拌反应1h,得到嵌段聚酰胺酸树脂溶液,备用;其中,体系中TFDB相对于BTDA单体过量,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数为5;The first step: take 32.621 parts of TFDB and 250 parts of aprotic polar solvent DMAc and put them in a three-necked flask with an electric stirrer, stir until completely dissolved, add 25.865 parts of BTDA monomer, and stir for 1 h to obtain a block polymer. An amic acid resin solution, for subsequent use; wherein, in the system, TFDB is excessive relative to BTDA monomer, and the number of repeating structural units in the obtained block polyamic acid resin solution is 5;

第二步:向所得嵌段聚酰胺酸树脂溶液中加入29.779份TPER和600份非质子极性溶剂DMAc,搅拌至单体完全溶解,然后加入62.671份BPADA单体(分3次加入),搅拌反应3h,得到低热膨胀系数可溶性聚酰胺酸树脂溶液,粘度为1.2万mpa·s;整个体系中二胺单体和二酐单体的摩尔比为1:1,嵌段聚酰胺酸树脂在体系中所占的比例为50mol%,固体含量15%;The second step: add 29.779 parts of TPER and 600 parts of aprotic polar solvent DMAc to the obtained block polyamic acid resin solution, stir until the monomer is completely dissolved, then add 62.671 parts of BPADA monomer (add in 3 times), stir The reaction was carried out for 3 hours to obtain a low thermal expansion coefficient soluble polyamic acid resin solution with a viscosity of 12,000 mpa·s; the molar ratio of diamine monomer and dianhydride monomer in the whole system was 1:1, and the block polyamic acid resin was in the system. The proportion of 50mol%, the solid content of 15%;

2)由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤:2) The steps of preparing low thermal expansion coefficient soluble polyimide resin powder from low thermal expansion coefficient soluble polyamic acid resin solution:

同实施例6。Same as Example 6.

所得低热膨胀系数可溶性聚酰亚胺树脂粉在有机溶剂中的溶解性如表1所示。Table 1 shows the solubility of the obtained low thermal expansion coefficient soluble polyimide resin powder in an organic solvent.

将本实施例所得低热膨胀系数可溶性聚酰亚胺树脂粉按实施例5中所述工艺制备低热膨胀系数可溶性聚酰亚胺薄膜。对所得薄膜的热膨胀系数等性能进行检测,结果如表1所示。The low-thermal-expansion-coefficient-soluble polyimide resin powder obtained in this example was used to prepare a low-thermal-expansion-coefficient-soluble polyimide film according to the process described in Example 5. The thermal expansion coefficient and other properties of the obtained films were tested, and the results are shown in Table 1.

实施例10Example 10

具体制备方法为:The specific preparation method is:

1)制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤:1) The steps of preparing the low thermal expansion coefficient soluble polyamic acid resin solution:

第一步:取39.765份的TFDB和250份非质子极性溶剂DMAc置于带有电动搅拌器的三口烧瓶中,搅拌至完全溶解,加入32.10份BTDA单体,搅拌反应1h,得到嵌段聚酰胺酸树脂溶液,备用;其中,体系中TFDB相对于BTDA单体过量,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数为5;The first step: take 39.765 parts of TFDB and 250 parts of aprotic polar solvent DMAc and place them in a three-necked flask with an electric stirrer, stir until completely dissolved, add 32.10 parts of BTDA monomer, and stir for 1 h to obtain a block polymer. An amic acid resin solution, for subsequent use; wherein, in the system, TFDB is excessive relative to BTDA monomer, and the number of repeating structural units in the obtained block polyamic acid resin solution is 5;

第二步:向所得嵌段聚酰胺酸树脂溶液中加入24.835份ODA和600份非质子极性溶剂DMAc,搅拌至单体完全溶解,然后加入54.397份OBDP单体(分3次加入),搅拌反应3h,得到低热膨胀系数可溶性聚酰胺酸树脂溶液,粘度为0.9万mpa·s;整个体系中二胺单体和二酐单体的摩尔比为1:1,嵌段聚酰胺酸树脂在体系中所占的比例为50mol%,固体含量15%;The second step: add 24.835 parts of ODA and 600 parts of aprotic polar solvent DMAc to the obtained block polyamic acid resin solution, stir until the monomer is completely dissolved, then add 54.397 parts of OBDP monomer (add in 3 times), stir The reaction was carried out for 3 hours to obtain a low thermal expansion coefficient soluble polyamic acid resin solution with a viscosity of 0.9 million mpa·s; the molar ratio of diamine monomer and dianhydride monomer in the whole system was 1:1, and the block polyamic acid resin was in the system. The proportion of 50mol%, the solid content of 15%;

2)由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤:2) The steps of preparing low thermal expansion coefficient soluble polyimide resin powder from low thermal expansion coefficient soluble polyamic acid resin solution:

同实施例6。Same as Example 6.

所得低热膨胀系数可溶性聚酰亚胺树脂粉在有机溶剂中的溶解性如表1所示。Table 1 shows the solubility of the obtained low thermal expansion coefficient soluble polyimide resin powder in an organic solvent.

将本实施例所得低热膨胀系数可溶性聚酰亚胺树脂粉按实施例5中所述工艺制备低热膨胀系数可溶性聚酰亚胺薄膜。对所得薄膜的热膨胀系数等性能进行检测,结果如表1所示。The low thermal expansion coefficient soluble polyimide resin powder obtained in this example is used to prepare a low thermal expansion coefficient soluble polyimide film according to the process described in Example 5. The thermal expansion coefficient and other properties of the obtained films were tested, and the results are shown in Table 1.

实施例11Example 11

具体制备方法为:The specific preparation method is:

1)制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤:1) The steps of preparing the low thermal expansion coefficient soluble polyamic acid resin solution:

第一步:取33.088份的TFDB和250份非质子极性溶剂DMAc置于带有电动搅拌器的三口烧瓶中,搅拌至完全溶解,加入22.168份NTCDA单体,搅拌反应1h,得到嵌段聚酰胺酸树脂溶液,备用;其中,体系中TFDB相对于NTCDA单体过量,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数为5;The first step: take 33.088 parts of TFDB and 250 parts of aprotic polar solvent DMAc and place them in a three-necked flask with an electric stirrer, stir until completely dissolved, add 22.168 parts of NTCDA monomer, and stir for 1 h to obtain a block polymer. The amic acid resin solution is for subsequent use; wherein, in the system, TFDB is excessive relative to the NTCDA monomer, and the number of repeating structural units in the obtained block polyamic acid resin solution is 5;

第二步:向所得嵌段聚酰胺酸树脂溶液中加入30.205份TPEQ和600份非质子极性溶剂DMAc,搅拌至单体完全溶解,然后加入64.537份BPADA单体(分3次加入),搅拌反应3h,得到低热膨胀系数可溶性聚酰胺酸树脂溶液,粘度为0.5万mpa·s;整个体系中二胺单体和二酐单体的摩尔比为1:1,嵌段聚酰胺酸树脂在体系中所占的比例为50mol%,固体含量15%;The second step: add 30.205 parts of TPEQ and 600 parts of aprotic polar solvent DMAc to the obtained block polyamic acid resin solution, stir until the monomer is completely dissolved, then add 64.537 parts of BPADA monomer (add in 3 times), stir Reaction for 3h to obtain a low thermal expansion coefficient soluble polyamic acid resin solution with a viscosity of 0.5 million mpa s; the molar ratio of diamine monomer and dianhydride monomer in the whole system is 1:1, and the block polyamic acid resin is in the system. The proportion of 50mol%, the solid content of 15%;

2)由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤:2) The steps of preparing low thermal expansion coefficient soluble polyimide resin powder from low thermal expansion coefficient soluble polyamic acid resin solution:

同实施例6。Same as Example 6.

所得低热膨胀系数可溶性聚酰亚胺树脂粉在有机溶剂中的溶解性如表1所示。Table 1 shows the solubility of the obtained low thermal expansion coefficient soluble polyimide resin powder in an organic solvent.

将本实施例所得低热膨胀系数可溶性聚酰亚胺树脂粉按实施例5中所述工艺制备低热膨胀系数可溶性聚酰亚胺薄膜。对所得薄膜的热膨胀系数等性能进行检测,结果如表1所示。The low thermal expansion coefficient soluble polyimide resin powder obtained in this example is used to prepare a low thermal expansion coefficient soluble polyimide film according to the process described in Example 5. The thermal expansion coefficient and other properties of the obtained films were tested, and the results are shown in Table 1.

对比例1Comparative Example 1

具体制备方法为:The specific preparation method is:

1)制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤:1) The steps of preparing the low thermal expansion coefficient soluble polyamic acid resin solution:

第一步:取31.543份的ODA和250份溶剂N,N-二甲基乙酰胺置于带有电动搅拌器的三口烧瓶中,搅拌至完全溶解,加入28.258份环己烷四酸二酐(HPMDA)单体,搅拌反应2h,得到嵌段聚酰胺酸树脂溶液,备用;其中,体系中二胺相对于HPMDA单体过量,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数为5;The first step: get 31.543 parts of ODA and 250 parts of solvent N,N-dimethylacetamide and place them in a three-necked flask with an electric stirrer, stir until completely dissolved, add 28.258 parts of cyclohexanetetracarboxylic dianhydride ( HPMDA) monomer, stirred and reacted for 2h to obtain a block polyamic acid resin solution, for subsequent use; wherein, the diamine in the system was excessive relative to the HPMDA monomer, and the number of repeating structural units in the obtained block polyamic acid resin solution was 5;

第二步:向所得嵌段聚酰胺酸树脂溶液中加入31.543份3,4-ODA和600非质子极性溶剂DMAc,搅拌至单体完全溶解,然后加入58.655份ODPA单体(分3次加入),搅拌反应4h,得到低热膨胀系数可溶性聚酰胺酸树脂溶液,粘度为0.9万mpa·s;整个体系中二胺单体和二酐单体的摩尔比为1:1,嵌段聚酰胺酸树脂在体系中所占的比例为50mol%,固体含量15%;The second step: add 31.543 parts of 3,4-ODA and 600 aprotic polar solvent DMAc to the obtained block polyamic acid resin solution, stir until the monomer is completely dissolved, then add 58.655 parts of ODPA monomer (add in 3 times ), stirred and reacted for 4 h to obtain a low thermal expansion coefficient soluble polyamic acid resin solution with a viscosity of 0.9 million mpa s; the molar ratio of diamine monomer and dianhydride monomer in the whole system was 1:1, and the block polyamic acid The proportion of resin in the system is 50mol%, and the solid content is 15%;

2)由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤:2) The steps of preparing low thermal expansion coefficient soluble polyimide resin powder from low thermal expansion coefficient soluble polyamic acid resin solution:

同实施例6。Same as Example 6.

所得低热膨胀系数可溶性聚酰亚胺树脂粉在有机溶剂中的溶解性如表1所示。Table 1 shows the solubility of the obtained low thermal expansion coefficient soluble polyimide resin powder in an organic solvent.

将本实施例所得低热膨胀系数可溶性聚酰亚胺树脂粉按实施例1中所述工艺制备低热膨胀系数可溶性聚酰亚胺薄膜。对所得薄膜的热膨胀系数等性能进行检测,结果如表1所示。The low-thermal-expansion-coefficient-soluble polyimide resin powder obtained in this example was used to prepare a low-thermal-expansion-coefficient-soluble polyimide film according to the process described in Example 1. The thermal expansion coefficient and other properties of the obtained films were tested, and the results are shown in Table 1.

对比例2Comparative Example 2

具体制备方法为:The specific preparation method is:

1)制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤:1) The steps of preparing the low thermal expansion coefficient soluble polyamic acid resin solution:

第一步:取26.596份的PBI和250份溶剂N,N-二甲基乙酰胺置于带有电动搅拌器的三口烧瓶中,搅拌至完全溶解,加入30.572份BPDA单体,搅拌反应2h,得到嵌段聚酰胺酸树脂溶液,备用;其中,体系中二胺相对于BPDA单体过量,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数为5;The first step: take 26.596 parts of PBI and 250 parts of solvent N,N-dimethylacetamide, put them in a three-necked flask with an electric stirrer, stir until completely dissolved, add 30.572 parts of BPDA monomer, and stir and react for 2h, Obtain block polyamic acid resin solution, standby; Wherein, in the system, diamine is excessive with respect to BPDA monomer, and the number of repeating structural units in the gained block polyamic acid resin solution is 5;

第二步:向所得嵌段聚酰胺酸树脂溶液中加入48.685份BAPP和600份非质子极性溶剂DMAc,搅拌至单体完全溶解,然后加入44.146份ODPA单体(分3次加入),搅拌反应4h,得到低热膨胀系数可溶性聚酰胺酸树脂溶液,粘度为1.2万mpa·s;整个体系中二胺单体和二酐单体的摩尔比为1:1,嵌段聚酰胺酸树脂在体系中所占的比例为50mol%,固体含量15%;The second step: add 48.685 parts of BAPP and 600 parts of aprotic polar solvent DMAc to the obtained block polyamic acid resin solution, stir until the monomer is completely dissolved, then add 44.146 parts of ODPA monomer (add in 3 times), stir After 4 hours of reaction, a low thermal expansion coefficient soluble polyamic acid resin solution was obtained, with a viscosity of 12,000 mpa·s; the molar ratio of diamine monomer and dianhydride monomer in the whole system was 1:1, and the block polyamic acid resin was in the system. The proportion of 50mol%, the solid content of 15%;

2)由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤:2) The steps of preparing low thermal expansion coefficient soluble polyimide resin powder from low thermal expansion coefficient soluble polyamic acid resin solution:

同实施例6。Same as Example 6.

所得低热膨胀系数可溶性聚酰亚胺树脂粉在有机溶剂中的溶解性如表1所示。Table 1 shows the solubility of the obtained low thermal expansion coefficient soluble polyimide resin powder in an organic solvent.

将本实施例所得低热膨胀系数可溶性聚酰亚胺树脂粉按实施例5中所述工艺制备低热膨胀系数可溶性聚酰亚胺薄膜。对所得薄膜的热膨胀系数等性能进行检测,结果如表1所示。The low thermal expansion coefficient soluble polyimide resin powder obtained in this example is used to prepare a low thermal expansion coefficient soluble polyimide film according to the process described in Example 5. The thermal expansion coefficient and other properties of the obtained films were tested, and the results are shown in Table 1.

对比例3Comparative Example 3

具体制备方法为:The specific preparation method is:

1)制备低热膨胀系数可溶性聚酰胺酸树脂溶液的步骤:1) The steps of preparing the low thermal expansion coefficient soluble polyamic acid resin solution:

第一步:取24.34份的3,4-ODA和250份溶剂N,N-二甲基乙酰胺置于带有电动搅拌器的三口烧瓶中,搅拌至完全溶解,加入28.644份BPDA单体,搅拌反应2h,得到嵌段聚酰胺酸树脂溶液,粘度为0.8万mpa·s,备用;其中,体系中二胺相对于BPDA单体过量,所得嵌段聚酰胺酸树脂溶液中的重复结构单元数为5;Step 1: Take 24.34 parts of 3,4-ODA and 250 parts of solvent N,N-dimethylacetamide and put them in a three-necked flask with an electric stirrer, stir until completely dissolved, add 28.644 parts of BPDA monomer, The reaction was stirred for 2h to obtain a block polyamic acid resin solution with a viscosity of 08,000 mPa·s, which was used for subsequent use; wherein, the diamine in the system was excessive relative to the BPDA monomer, and the number of repeating structural units in the obtained block polyamic acid resin solution was is 5;

第二步:向所得嵌段聚酰胺酸树脂溶液中加入49.958份BAPP和600份非质子极性溶剂DMAc,搅拌至单体完全溶解,然后加入47.057份BTDA单体(分3次加入),搅拌反应4h,得到低热膨胀系数可溶性聚酰胺酸树脂溶液,粘度为2.6mpa·s;整个体系中二胺单体和二酐单体的摩尔比为1:1,嵌段聚酰胺酸树脂在体系中所占的比例为40mol%,固体含量15%;The second step: add 49.958 parts of BAPP and 600 parts of aprotic polar solvent DMAc to the obtained block polyamic acid resin solution, stir until the monomer is completely dissolved, then add 47.057 parts of BTDA monomer (add in 3 times), stir After 4 hours of reaction, a low thermal expansion coefficient soluble polyamic acid resin solution was obtained, with a viscosity of 2.6 mpa·s; the molar ratio of diamine monomer and dianhydride monomer in the whole system was 1:1, and the block polyamic acid resin was in the system. The proportion is 40mol%, and the solid content is 15%;

2)由低热膨胀系数可溶性聚酰胺酸树脂溶液制备低热膨胀系数可溶性聚酰亚胺树脂粉的步骤:2) The steps of preparing low thermal expansion coefficient soluble polyimide resin powder from low thermal expansion coefficient soluble polyamic acid resin solution:

同实施例6。Same as Example 6.

所得低热膨胀系数可溶性聚酰亚胺树脂粉在有机溶剂中的溶解性如表1所示。Table 1 shows the solubility of the obtained low thermal expansion coefficient soluble polyimide resin powder in an organic solvent.

将本实施例所得低热膨胀系数可溶性聚酰亚胺树脂粉按实施例1中所述工艺制备低热膨胀系数可溶性聚酰亚胺薄膜。对所得薄膜的热膨胀系数等性能进行检测,结果如表1所示。The low-thermal-expansion-coefficient-soluble polyimide resin powder obtained in this example was used to prepare a low-thermal-expansion-coefficient-soluble polyimide film according to the process described in Example 1. The thermal expansion coefficient and other properties of the obtained films were tested, and the results are shown in Table 1.

表1:Table 1:

Figure BDA0002284320420000161
Figure BDA0002284320420000161

注:-表示加热可溶,--表示可溶,○不可溶;热膨胀系数取值范围100~200℃,a为嵌段聚酰胺酸树脂溶液中的重复结构单元数。Note: - means soluble by heating, -- means soluble, ○ is insoluble; the thermal expansion coefficient ranges from 100 to 200°C, and a is the number of repeating structural units in the block polyamic acid resin solution.

对比实施例1~11和对比例1,采用六元环结构的HPMDA制备的聚酰亚胺树脂粉,虽然具有可溶性,但其耐热性不足,在100~200℃范围内CTE偏高为46.4ppm/K;对比例2采用含有杂化结构的PBI,CTE值较低,可溶性不足;对比例3与实施例6对比发现,将TFDB替换为ODA,不仅可溶性降低,CTE值也变高。Comparing Examples 1 to 11 and Comparative Example 1, the polyimide resin powder prepared by HPMDA with a six-membered ring structure is soluble, but its heat resistance is insufficient, and the CTE is 46.4 in the range of 100 to 200 ° C. ppm/K; Comparative Example 2 uses PBI with a hybrid structure, which has a low CTE value and insufficient solubility; Comparative Example 3 is compared with Example 6, and it is found that replacing TFDB with ODA not only reduces the solubility, but also increases the CTE value.

Claims (9)

1. A soluble polyimide resin powder with low thermal expansion coefficient has a molecular structure shown as the following formula (A):
Figure FDA0002284320410000011
wherein:
the molar ratio of diamine groups to dianhydride groups in formula (a) is 1: 1;
ar1 represents any one of the following formulae (Ar1-1) to (Ar1-8) and isomers thereof:
Figure FDA0002284320410000012
ar2 represents any one of the following formulae (Ar2-1) to (Ar2-10) and isomers thereof:
Figure FDA0002284320410000013
d represents a rigid linear block, the proportion of the block in the total molecular structure represented by the formula (A) is 15 to 60 mol%, and the block is composed of a repeating structural unit represented by the following formula (B):
Figure FDA0002284320410000021
wherein,
a=2~20;
ar3 represents any one of the following formulae (Ar3-1) to (Ar3-5) and isomers thereof:
Figure FDA0002284320410000022
2. the method for preparing a low cte soluble polyimide resin powder of claim 1, comprising the steps of preparing a low cte soluble polyamic acid resin solution and preparing a low cte soluble polyimide resin powder from the low cte soluble polyamic acid resin solution, wherein: the step of preparing the soluble polyamic acid resin solution with low thermal expansion coefficient includes:
the first step is as follows: reacting 4,4 '-diamino-2, 2' -bistrifluoromethylbiphenyl with a dianhydride monomer with a main structure of Ar3 in an aprotic polar solvent to obtain a block polyamic acid resin solution; wherein,
ar3 represents any one of the following formulae (Ar3-1) to (Ar3-5) and isomers thereof:
Figure FDA0002284320410000023
the second step is that: adding a diamine monomer with a main structure of Ar1 and an aprotic polar solvent into the obtained block polyamic acid resin solution, and then adding a dianhydride monomer with a main structure of Ar2 in batches for reaction to obtain a soluble polyamic acid resin solution with a low thermal expansion coefficient; wherein,
the adding amount of the diamine monomer with the main structure of Ar1 and the dianhydride monomer with the main structure of Ar2 is controlled to be 15-60 mol% of the block polyamic acid resin in the obtained low-thermal expansion coefficient soluble polyamic acid resin, and the adding amount of the dianhydride monomer with the main structure of Ar2 and the diamine monomer with the main structure of Ar1 enables the molar ratio of diamine groups and dianhydride groups in the obtained low-thermal expansion coefficient soluble polyamic acid resin to be 1: 1;
ar1 represents any one of the following formulae (Ar1-1) to (Ar1-8) and isomers thereof:
Figure FDA0002284320410000031
ar2 represents any one of the following formulae (Ar2-1) to (Ar2-10) and isomers thereof:
Figure FDA0002284320410000032
3. the method of claim 2, wherein: the dianhydride monomer with the main structure of Ar3 is selected from pyromellitic dianhydride (PMDA), 3,3',4,4' -biphenyl tetracarboxylic dianhydride, 2,3,3',4' -biphenyl tetracarboxylic dianhydride, benzophenone tetracarboxylic dianhydride and 1,4,5, 8-naphthalene tetracarboxylic dianhydride.
4. The method of claim 2, wherein: the diamine monomer with the main structure of Ar1 is selected from 3, 4-diaminodiphenyl ether, 3' diaminodiphenyl ether, 4-diaminodiphenyl ether, 2-bis [4- (4-aminophenoxy) phenyl ] propane, all-meta-triphenyldiethanediamine, 1, 3-bis (4-aminophenoxy) benzene, 3, 5-diamino 4' -phenylalkynylbenzophenone, N ' -diphenylbiphenyldiamine, 3' -diaminobenzophenone, 4' -diaminodiphenyldifluoromethane, 2-bis (4-aminophenyl) -propane, bis (4- (3-aminophenoxy) phenyl) sulfide, 4' -diaminodiphenylsulfide, 3, 4' -diaminodiphenylsulfide and bis (4- (3-aminophenoxy) phenyl) sulfone, 1, 6-hexanediamine, 1, 9-nonanediamine and 1, 10-diaminodecane.
5. The method of claim 2, wherein: the dianhydride monomer with the main structure of Ar2 is any one selected from 3,3',4,4' -biphenyl tetracarboxylic dianhydride, 2,3,3',4' -biphenyl tetracarboxylic dianhydride, 3,3',4,4' -diphenyl sulfone tetracarboxylic dianhydride, butane tetracarboxylic dianhydride, cyclohexane tetracarboxylic dianhydride, 3,3',4,4' -diphenyl ether tetracarboxylic dianhydride, 4, 4-hexafluoroisopropyl phthalic anhydride, benzophenone tetracarboxylic dianhydride, bisphenol A type diether dianhydride and triphenyl diether dianhydride.
6. The production method according to any one of claims 2 to 5, characterized in that: the preparation method of the low thermal expansion coefficient soluble polyimide resin powder from the low thermal expansion coefficient soluble polyamic acid resin solution comprises the following steps: imidizing the low-thermal expansion coefficient soluble polyamic acid resin solution in a chemical imidization mode or a thermal imidization mode to obtain low-thermal expansion coefficient soluble polyimide resin powder; wherein the imidization is carried out at a temperature of less than or equal to 250 ℃.
7. The method of claim 6, wherein: the imidization is carried out at the temperature of less than or equal to 200 ℃.
8. The method of claim 6, wherein: when imidization is carried out in a chemical imidization mode, the step of preparing the low-thermal expansion coefficient soluble polyimide resin powder from the low-thermal expansion coefficient soluble polyamic acid resin solution comprises the following steps:
placing the low-thermal-expansion-coefficient soluble polyamic acid resin solution into a reaction container, adding an amine catalyst, a dehydrating agent and xylene into the reaction container, controlling the solid content of the low-thermal-expansion-coefficient soluble polyamic acid resin in the obtained system to be 5-10%, then reacting under heating or non-heating conditions, cooling after the reaction is finished, transferring the reaction material into a poor solvent, filtering, and imidizing a filter cake under the conditions of vacuum and the temperature of less than or equal to 250 ℃ to obtain the low-thermal-expansion-coefficient soluble polyimide resin powder.
9. The method of claim 6, wherein: when imidization is carried out in a thermal imidization mode, the step of preparing the low-thermal expansion coefficient soluble polyimide resin powder from the low-thermal expansion coefficient soluble polyamic acid resin solution comprises the following steps:
placing the low-thermal-expansion-coefficient soluble polyamic acid resin solution into a reaction container, adding xylene into the reaction container, controlling the solid content of the low-thermal-expansion-coefficient soluble polyamic acid resin in the obtained system to be 5-10%, then reacting under a heating condition, cooling after the reaction is finished, transferring the reaction material into a poor solvent, filtering, and imidizing a filter cake under the conditions of vacuum and the temperature of less than or equal to 250 ℃ to obtain the low-thermal-expansion-coefficient soluble polyimide resin powder.
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Application publication date: 20200417