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CN101654518B - Thermosetting polyimide resin and preparation method and application thereof - Google Patents

Thermosetting polyimide resin and preparation method and application thereof Download PDF

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CN101654518B
CN101654518B CN2009100939220A CN200910093922A CN101654518B CN 101654518 B CN101654518 B CN 101654518B CN 2009100939220 A CN2009100939220 A CN 2009100939220A CN 200910093922 A CN200910093922 A CN 200910093922A CN 101654518 B CN101654518 B CN 101654518B
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杨士勇
曲希明
冀棉
范琳
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Abstract

本发明公开了一种降冰片烯封端的聚酰亚胺树脂及其制备方法与应用。该聚酰亚胺树脂的结构式如式I所示。本发明的聚酰亚胺树脂是以反应性封端剂、芳香族四酸二酐和芳香族二胺为原料,采用PMR方法制备得到的。本发明所提供的聚酰亚胺树脂还可经热处理后得到树脂模塑粉,模塑粉具有低的熔体粘度,经热固化后得到力学性能高、耐热性能优良的纯树脂模压件。所述的聚酰亚胺树脂适于浸渍碳纤维、玻璃纤维或芳纶纤维等,制成预浸料;该预浸料具有良好的成型加工性能,采用热模压或真空热压罐工艺经50-320℃的热固化成型后可得到孔隙率低、力学性能高、耐热性能优良的复合材料。该复合材料可用于制备航空、航天、空间技术等领域的耐高温零部件,在350-370℃环境下长期使用。

Figure 200910093922.0_AB_0
式IThe invention discloses a norbornene-terminated polyimide resin, a preparation method and application thereof. The structural formula of the polyimide resin is shown in Formula I. The polyimide resin of the invention is prepared by using a reactive end-capping agent, an aromatic tetra-acid dianhydride and an aromatic diamine as raw materials by a PMR method. The polyimide resin provided by the invention can also be heat-treated to obtain resin molding powder. The molding powder has low melt viscosity, and after heat curing, a pure resin molded part with high mechanical properties and excellent heat resistance can be obtained. The polyimide resin is suitable for impregnating carbon fiber, glass fiber or aramid fiber, etc., to make a prepreg; the prepreg has good molding performance, and it can be processed by hot molding or vacuum autoclave after 50- Composite materials with low porosity, high mechanical properties and excellent heat resistance can be obtained after thermosetting molding at 320 °C. The composite material can be used to prepare high-temperature-resistant components in the fields of aviation, aerospace, space technology, etc., and can be used for a long time under the environment of 350-370°C.
Figure 200910093922.0_AB_0
Formula I

Description

一种热固性聚酰亚胺树脂及其制备方法与应用 A kind of thermosetting polyimide resin and its preparation method and application

技术领域technical field

本发明涉及一种热固性聚酰亚胺树脂及其制备方法与应用。The invention relates to a thermosetting polyimide resin and its preparation method and application.

背景技术Background technique

热固性聚酰亚胺树脂具有高的玻璃化温度、优异的耐热氧化稳定性和力学性能,以其为树脂基体与碳纤维复合制备的复合材料是目前耐温等级最高的树脂基复合材料,作为质轻、耐高温的结构件在航空、航天、空间技术等领域具有重要的应用价值。按照所采用的反应性封端剂的种类,热固性聚酰亚胺树脂主要分为双马来酰亚胺树脂、PMR型聚酰亚胺树脂和苯炔基封端的聚酰亚胺树脂等三大类,其中最具代表性的PMR型聚酰亚胺树脂为PMR-15树脂(U.S.Patent 3,745,149),其耐热等级为316℃,由其与碳纤维复合制备的复合材料可在316℃的高温下长期使用。PMR-II-50(NASA-TM-X-71894)具有更高的耐热性能,其耐热等级为371℃。但是,该树脂由于熔融性能差,成型工艺性能低,难于制备大型或复杂形状的复合材料构件。Thermosetting polyimide resin has a high glass transition temperature, excellent heat-resistant oxidation stability and mechanical properties. The composite material prepared by combining it with carbon fiber is the resin-based composite material with the highest temperature resistance level. As a quality Lightweight and high temperature resistant structural parts have important application value in aviation, aerospace, space technology and other fields. According to the type of reactive end-capping agent used, thermosetting polyimide resin is mainly divided into three major types: bismaleimide resin, PMR type polyimide resin and phenynyl-terminated polyimide resin. Among them, the most representative PMR type polyimide resin is PMR-15 resin (U.S. Patent 3,745,149), its heat resistance grade is 316°C, and the composite material prepared by combining it with carbon fiber can be used at a high temperature of 316°C long-term use. PMR-II-50 (NASA-TM-X-71894) has higher heat resistance, and its heat resistance grade is 371°C. However, the resin has poor melting performance and low molding process performance, making it difficult to prepare large or complex-shaped composite material components.

近年来,人们发现含不对称联苯酰亚胺结构的热固性聚酰亚胺树脂具有优良的熔融性能包括低的熔体粘度和熔融温度及良好的熔体稳定性,同时其热固化物具有较高的耐热性能。美国专利(U.S.Patent 5,432,001、U.S.Patent 5,461,138、U.S.Patent5,461,137)公开了降冰片烯二甲酸酐为封端剂,含有不对称联苯酰亚胺结构的聚酰亚胺树脂。但是,这些树脂加热熔融后的熔体粘度高,只能适于热模压成型工艺在320℃高温下制备碳纤维增强复合材料。美国专利(U.S.Patent 7,015,304B1)公开了一种苯乙炔基封端的,含有不对称联苯酰亚胺结构的聚酰亚胺树脂,该树脂具有很低的熔体粘度,可适于树脂传递成型工艺,用于制备耐288-343℃的碳纤维增强复合材料。但是,这种树脂需要在更高的温度下(>370℃)才能完成热固化交联反应。In recent years, it has been found that thermosetting polyimide resins containing asymmetric biphenylimide structures have excellent melting properties including low melt viscosity and melting temperature and good melt stability, while their thermosetting products have relatively High heat resistance. U.S. Patents (U.S.Patent 5,432,001, U.S.Patent 5,461,138, U.S.Patent 5,461,137) disclose norbornene dicarboxylic anhydride as a capping agent and a polyimide resin containing an asymmetric biphenylimide structure. However, these resins have high melt viscosity after heating and melting, so they are only suitable for the preparation of carbon fiber reinforced composite materials at a high temperature of 320 ° C by thermal molding process. U.S. Patent 7,015,304B1 discloses a phenylethynyl-terminated polyimide resin containing an asymmetric biphenylimide structure, which has a very low melt viscosity and is suitable for resin transfer molding Process for the preparation of carbon fiber reinforced composite materials resistant to 288-343 °C. However, this resin requires a higher temperature (>370°C) to complete the thermal curing crosslinking reaction.

因此,发展具有优良熔融性能、低固化温度、高耐热性能和高力学性能的聚酰亚胺树脂对于发展耐高温碳纤维增强复合材料具有重要意义。Therefore, the development of polyimide resins with excellent melting properties, low curing temperature, high heat resistance and high mechanical properties is of great significance for the development of high temperature resistant carbon fiber reinforced composite materials.

发明内容Contents of the invention

本发明的目的是提供一种热固性聚酰亚胺树脂及其制备方法。The object of the present invention is to provide a kind of thermosetting polyimide resin and preparation method thereof.

本发明所提供的是一种具有低熔体粘度、高耐热性能的热固性聚酰亚胺树脂,该聚酰亚胺树脂不仅适于热模压成型工艺,而且还适于热压罐成型工艺,在320℃高温下成型制备的纤维增强复合材料具有优良的耐热性能和综合力学性能。The present invention provides a thermosetting polyimide resin with low melt viscosity and high heat resistance. The polyimide resin is not only suitable for thermocompression molding process, but also suitable for autoclave molding process. The fiber-reinforced composite material prepared at a high temperature of 320°C has excellent heat resistance and comprehensive mechanical properties.

本发明所提供的聚酰亚胺树脂的结构通式如式I所示,The structural general formula of polyimide resin provided by the present invention is as shown in formula I,

(式I)(Formula I)

式I中,In formula I,

Figure G2009100939220D00023
or
Figure G2009100939220D00023

Figure G2009100939220D00024
Figure G2009100939220D00024

Figure G2009100939220D00025
Figure G2009100939220D00026
Figure G2009100939220D00025
or
Figure G2009100939220D00026

Figure G2009100939220D00031
Figure G2009100939220D00032
Figure G2009100939220D00031
or
Figure G2009100939220D00032

所述m=1-20,n=0.01-6。Said m=1-20, n=0.01-6.

根据所用的封端剂、芳香族四酸二酐和芳香族二胺的比例计算得到所述聚酰亚胺树脂的数均分子量为1000-9000(由于聚酰亚胺的溶解性差,无法用实验方法测定分子量)。According to the ratio of end-capping agent used, aromatic tetra-acid dianhydride and aromatic diamine, the number-average molecular weight of the polyimide resin is calculated to be 1000-9000 (due to the poor solubility of polyimide, it cannot be obtained by experiment method to determine the molecular weight).

上述聚酰亚胺树脂的制备方法,包括以下步骤:The preparation method of above-mentioned polyimide resin comprises the following steps:

1)将封端剂与有机脂肪醇溶剂进行酯化反应,得到封端剂单酸单酯溶液;1) Esterifying the end-capping agent with an organic aliphatic alcohol solvent to obtain a monoacid monoester solution of the end-capping agent;

2)将芳香族四酸二酐与有机脂肪醇溶剂进行酯化反应,得到芳香族四酸二酯溶液;2) Esterifying the aromatic tetra-acid dianhydride with an organic aliphatic alcohol solvent to obtain an aromatic tetra-acid diester solution;

3)将芳香族二胺溶解于有机脂肪醇溶剂中,然后依次加入步骤1)的封端剂单酸单酯溶液、步骤2)的芳香族四酸二酯溶液进行反应,得到式I所示的聚酰亚胺树脂溶液;3) dissolving the aromatic diamine in an organic aliphatic alcohol solvent, then adding the end-capping agent monoacid monoester solution in step 1) and the aromatic tetraacid diester solution in step 2) to react to obtain the formula shown in I The polyimide resin solution;

其中,所述封端剂为式II所示的化合物,Wherein, the capping agent is a compound shown in formula II,

Figure G2009100939220D00033
Figure G2009100939220D00033

(式II);(Formula II);

所述芳香族四酸二酐为下述芳香族四酸二酐I与芳香族四酸二酐II的混合物,其中,芳香族四酸二酐I与芳香族四酸二酐II的质量份数比为100∶1-30;The aromatic tetra-acid dianhydride is a mixture of the following aromatic tetra-acid dianhydride I and aromatic tetra-acid dianhydride II, wherein the mass fraction of aromatic tetra-acid dianhydride I and aromatic tetra-acid dianhydride II The ratio is 100:1-30;

所述芳香族四酸二酐I选自下述式A1、式A2、式A3所示化合物中的一种:The aromatic tetra-acid dianhydride I is selected from one of the compounds shown in the following formula A1, formula A2, and formula A3:

Figure G2009100939220D00034
Figure G2009100939220D00034

式A1                        式A2                        式A3Formula A1 Formula A2 Formula A3

所述芳香族四酸二酐II选自下述式B1、式B2、式B3所示化合物中的一种:The aromatic tetra-acid dianhydride II is selected from one of the compounds shown in the following formula B1, formula B2, and formula B3:

Figure G2009100939220D00041
Figure G2009100939220D00041

式B1                          式B2                       式B3Formula B1 Formula B2 Formula B3

所述芳香族二胺选自下述化合物中的一种:The aromatic diamine is selected from one of the following compounds:

Figure G2009100939220D00042
Figure G2009100939220D00042

对苯二胺      间苯二胺      4,4’-二氨基联苯       4,4’-二氨基二苯醚p-phenylenediamine m-phenylenediamine 4,4'-diaminobenzidine 4,4'-diaminodiphenyl ether

Figure G2009100939220D00044
Figure G2009100939220D00045
Figure G2009100939220D00044
Figure G2009100939220D00045

3,4’-二氨基二苯醚   4,4’-二氨基二苯甲烷     4,4’-二氨基二苯甲酮3,4'-diaminodiphenyl ether 4,4'-diaminodiphenylmethane 4,4'-diaminobenzophenone

Figure G2009100939220D00046
Figure G2009100939220D00047
                
Figure G2009100939220D00048
Figure G2009100939220D00046
Figure G2009100939220D00047
                
Figure G2009100939220D00048

4,4’-二氨基二苯砜   2,2’-二甲基-4,4’-二氨基联苯   2,2’-二三氟甲基-4,4’-二氨基联苯4,4'-Diaminodiphenylsulfone 2,2'-Dimethyl-4,4'-diaminobiphenyl 2,2'-Ditrifluoromethyl-4,4'-diaminobiphenyl

Figure G2009100939220D00049
                       
Figure G2009100939220D000410
Figure G2009100939220D00049
                       
Figure G2009100939220D000410

2,2’,6,6’-四甲基-4,4’-二氨基联苯  2,2-双(4-(4-氨基苯氧基)苯基)丙烷2,2',6,6'-tetramethyl-4,4'-diaminobiphenyl 2,2-bis(4-(4-aminophenoxy)phenyl)propane

                      

Figure G2009100939220D000412
                      
Figure G2009100939220D000412

2,2-双(4-(4-氨基苯基)六氟丙烷           2,2-双(4-(4-氨基苯氧基)苯基)六氟丙烷2,2-bis(4-(4-aminophenyl)hexafluoropropane 2,2-bis(4-(4-aminophenoxy)phenyl)hexafluoropropane

Figure G2009100939220D000413
Figure G2009100939220D000413

1,4-双(4-氨基苯氧基)            1,3-双(4-氨基苯氧基)苯1,4-bis(4-aminophenoxy) 1,3-bis(4-aminophenoxy)benzene

Figure G2009100939220D000414
           
Figure G2009100939220D000415
Figure G2009100939220D000414
           
Figure G2009100939220D000415

1,3-双(3-氨基苯氧基)苯                  1,4-双(4-氨基-2-三氟甲基苯氧基)苯1,3-bis(3-aminophenoxy)benzene 1,4-bis(4-amino-2-trifluoromethylphenoxy)benzene

Figure G2009100939220D000416
     
Figure G2009100939220D000417
Figure G2009100939220D000416
Figure G2009100939220D000417
;

4,4’-双(4-氨基苯氧基)联苯             4,4’-双(4-氨基-2-三氟甲基苯氧基)联苯4,4'-bis(4-aminophenoxy)biphenyl 4,4'-bis(4-amino-2-trifluoromethylphenoxy)biphenyl

所述封端剂、芳香族四酸二酐和芳香族二胺的质量份数比依次为5-80∶100∶30-150。The ratio of the number of parts by mass of the end-capping agent, aromatic tetra-acid dianhydride and aromatic diamine is 5-80:100:30-150 in sequence.

步骤3)中所述反应的反应温度为5-40℃,反应时间为1-10小时。The reaction temperature of the reaction in step 3) is 5-40° C., and the reaction time is 1-10 hours.

其中,步骤1)、步骤2)和步骤3)中所述有机脂肪醇溶剂为下述醇中的至少一种甲醇、乙醇、丙醇、异丙醇、正丁醇、异丁醇、正戊醇、异戊醇、叔丁醇;或为上述醇中的一种与下述至少一种溶剂的任意比例混合的混合物:丙酮、四氢呋喃、二氧六环、苯、甲苯、氯仿和二氯甲烷。Wherein, the organic fatty alcohol solvent described in step 1), step 2) and step 3) is at least one of methanol, ethanol, propanol, isopropanol, n-butanol, isobutanol, n-pentyl alcohol in the following alcohols Alcohol, isoamyl alcohol, tert-butanol; or a mixture of one of the above alcohols mixed with at least one of the following solvents in any proportion: acetone, tetrahydrofuran, dioxane, benzene, toluene, chloroform and methylene chloride .

步骤1)中所述封端剂与有机脂肪醇溶剂的质量份数比可为5-80∶5-600;1)中所述酯化反应在65-140℃加热回流的条件下进行,反应时间可为1-6小时。The mass fraction ratio of the capping agent and the organic aliphatic alcohol solvent in step 1) can be 5-80:5-600; the esterification reaction described in 1) is carried out under the condition of heating and refluxing at 65-140°C, and the reaction The time can be 1-6 hours.

步骤2)中所述芳香族四酸二酐与有机脂肪醇溶剂的质量份数比可为100∶60-1200;步骤2)中所述酯化反应在65-140℃加热回流的条件下进行,反应时间可为1-6小时。The mass fraction ratio of the aromatic tetra-acid dianhydride to the organic aliphatic alcohol solvent in step 2) can be 100:60-1200; the esterification reaction in step 2) is carried out under the condition of heating and refluxing at 65-140°C , The reaction time can be 1-6 hours.

步骤3)中所述芳香族二胺与有机脂肪醇溶剂的质量份数可比为30-150∶10-800。The mass fraction of aromatic diamine and organic aliphatic alcohol solvent described in step 3) can be 30-150:10-800.

本发明所提供的聚酰亚胺树脂的溶液还可经热处理后得到树脂模塑粉(即固态的聚酰亚胺树脂),模塑粉具有低的熔体粘度,经热固化后得到力学性能高、耐热性能优良的纯树脂模压件。The solution of polyimide resin provided by the present invention can also obtain resin molding powder (i.e. solid polyimide resin) after heat treatment, and molding powder has low melt viscosity, obtains mechanical properties after thermosetting Pure resin molded parts with high heat resistance and excellent performance.

本发明的再一个目的是提供式I所示的聚酰亚胺树脂在制备聚酰亚胺树脂基复合材料中的应用。本发明所述的聚酰亚胺树脂适于浸渍碳纤维、玻璃纤维或芳纶纤维等,制成预浸料(带或布);该预浸料具有良好的成型加工性能,采用热模压或真空热压罐工艺经50-320℃的热固化成型后可得到孔隙率低、力学性能高、耐热性能优良的复合材料。所述复合材料的玻璃化温度在350-450℃之间,可用于制备航空、航天、空间技术等领域的耐高温零部件,在350-370℃环境下长期使用。Another object of the present invention is to provide the application of the polyimide resin represented by formula I in the preparation of polyimide resin-based composite materials. The polyimide resin of the present invention is suitable for impregnating carbon fiber, glass fiber or aramid fiber etc. to make prepreg (tape or cloth); Composite materials with low porosity, high mechanical properties and excellent heat resistance can be obtained after thermosetting molding at 50-320 °C in the autoclave process. The glass transition temperature of the composite material is between 350-450°C, it can be used to prepare high-temperature-resistant components in the fields of aviation, aerospace, space technology, etc., and it can be used for a long time under the environment of 350-370°C.

具体实施方式Detailed ways

下述实施例中所述实验方法,如无特殊说明,均为常规方法;所述试剂和材料,如无特殊说明,均可从商业途径获得。The experimental methods described in the following examples, unless otherwise specified, are conventional methods; the reagents and materials, unless otherwise specified, can be obtained from commercial sources.

下述实施例中的A1、A2、A3、B1、B2、B3化合物的结构式如下:The structural formulas of A1, A2, A3, B1, B2, B3 compounds in the following examples are as follows:

Figure G2009100939220D00051
Figure G2009100939220D00051

实施例1、聚酰亚胺树脂的制备以及树脂模压件的性能Embodiment 1, the preparation of polyimide resin and the performance of resin molding

1)将36质量份封端剂降冰片烯二甲酸酐在48质量份乙醇中86℃加热回流4小时得到降冰片烯二甲酸单酯溶液(NE)。1) 36 parts by mass of the capping agent norbornene dicarboxylic anhydride was heated to reflux at 86° C. for 4 hours in 48 parts by mass of ethanol to obtain a norbornene dicarboxylic acid monoester solution (NE).

2)将90质量份化合物A1在135质量份乙醇中83℃加热回流3小时得到化合物A1的酯化物溶液,将10质量份化合物B1在15质量份乙醇中85℃加热回流4小时得到化合物B1的酯化物溶液。2) Heat reflux 90 parts by mass of compound A 1 in 135 parts by mass of ethanol at 83°C for 3 hours to obtain an esterified solution of compound A 1 , and heat reflux 10 parts by mass of compound B 1 in 15 parts by mass of ethanol at 85°C for 4 hours to obtain The esterification product solution of compound B1 .

3)将50质量份间苯二胺溶解在68质量份乙醇中,搅拌半小时后依次加入上述制备的NE、化合物A1和B1的酯化物溶液,在20℃下搅拌反应8小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为1530,式I中m为2.79,n为0.28。3) Dissolve 50 parts by mass of m-phenylenediamine in 68 parts by mass of ethanol, stir for half an hour, then add the above-prepared NE, the esterification solution of compounds A1 and B1 in sequence, and stir and react at 20°C for 8 hours to obtain The homogeneous polyimide matrix resin solution has a calculated number average molecular weight of 1530, m in formula I is 2.79, and n is 0.28.

将步骤3)得到的树脂溶液依次经70℃/3h、140℃/2h、200℃/1h升温热处理,得到树脂模塑粉,测得其最低熔体粘度为70Pa.s;将该模塑粉在250-320℃和2MPa压力下热固化后得到纯树脂模压件,该树脂模压件的玻璃化转变温度大于380℃(采用DMA法测定),拉伸强度大于85MPa,弯曲强度大于130MPa。The resin solution obtained in step 3) is heated and heat-treated at 70°C/3h, 140°C/2h, and 200°C/1h to obtain resin molding powder, and its minimum melt viscosity is measured to be 70Pa.s; the molding powder After thermal curing at 250-320°C and 2MPa pressure, a pure resin molded part can be obtained. The glass transition temperature of the resin molded part is greater than 380°C (measured by DMA method), the tensile strength is greater than 85MPa, and the bending strength is greater than 130MPa.

实施例2、聚酰亚胺树脂的制备以及碳纤维聚酰亚胺复合材料层压板的性能Embodiment 2, the preparation of polyimide resin and the performance of carbon fiber polyimide composite laminate

1)将28质量份封端剂降冰片烯二甲酸酐在31质量份甲醇中68℃加热回流2小时得到相应的降冰片烯二甲酸单酯溶液(NE)。1) 28 parts by mass of the capping agent norbornene dicarboxylic anhydride were heated to reflux at 68° C. for 2 hours in 31 parts by mass of methanol to obtain the corresponding norbornene dicarboxylic acid monoester solution (NE).

2)将72质量份化合物A1在80质量份甲醇中69℃加热回流3小时得到化合物A1的酯化物溶液,将9份化合物B2在9质量份甲醇中70℃加热回流5小时得到化合物B2的酯化物溶液。2) Heat 72 parts by mass of compound A 1 in 80 parts by mass of methanol to reflux at 69°C for 3 hours to obtain an esterification product solution of compound A 1 , and heat 9 parts by mass of compound B 2 to reflux at 70°C in 9 parts by mass of methanol for 5 hours to obtain compound Esterate solution of B2 .

3)将72质量份3,4’-二氨基二苯醚溶解在60质量份甲醇中,搅拌半小时后依次加入NE、化合物A1和B2的酯化物溶液,在30℃下搅拌5小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为1970,式I中m为2.87,n为0.34。3) Dissolve 72 parts by mass of 3,4'-diaminodiphenyl ether in 60 parts by mass of methanol, stir for half an hour, then add NE, the esterified solution of compounds A 1 and B 2 in sequence, and stir at 30°C for 5 hours , to obtain a homogeneous polyimide matrix resin solution, the calculated number average molecular weight is 1970, m in formula I is 2.87, and n is 0.34.

将步骤3)得到的树脂溶液在缠绕机上与碳纤维进行复合制备预浸料,对预浸料进行裁剪、铺层,在50-320℃和3MPa压力下热固化后得到碳纤维聚酰亚胺复合材料层压板。Compound the resin solution obtained in step 3) with carbon fiber on a winding machine to prepare a prepreg, cut and lay up the prepreg, and heat-cure at 50-320°C and 3MPa pressure to obtain a carbon fiber polyimide composite material laminate.

测得该层压板的玻璃化转变温度大于360℃(采用DMA法测定),弯曲强度大于1400MPa,弯曲模量大于100GPa,层间剪切强度大于80MPa。It is measured that the glass transition temperature of the laminate is greater than 360° C. (measured by DMA method), the bending strength is greater than 1400 MPa, the flexural modulus is greater than 100 GPa, and the interlaminar shear strength is greater than 80 MPa.

实施例3、聚酰亚胺树脂的制备以及树脂模压件的性能Embodiment 3, the preparation of polyimide resin and the performance of resin molding

1)将19质量份封端剂降冰片烯二甲酸酐在22质量份甲醇中70℃加热回流2小时得到降冰片烯二甲酸单酯溶液(NE)。1) 19 parts by mass of end-capping agent norbornene dicarboxylic anhydride was heated to reflux at 70° C. for 2 hours in 22 parts by mass of methanol to obtain norbornene dicarboxylic acid monoester solution (NE).

2)将37质量份化合物A2在52质量份乙醇中84℃加热回流5小时得到化合物A2的酯化物溶液,将9质量份化合物B1在13质量份乙醇中85℃加热回流2小时得到化合物B1的酯化物溶液。2) Heat 37 parts by mass of Compound A 2 in 52 parts by mass of ethanol at 84°C for 5 hours to obtain an esterified product solution of Compound A 2 , and heat 9 parts by mass of Compound B 1 in 13 parts by mass of ethanol at 85°C for 2 hours to obtain The esterification product solution of compound B1 .

3)将45质量份4,4’-二氨基二苯甲烷溶解在34质量份甲醇中,搅拌半小时后依次加入上述NE、化合物A2和B1的酯化物溶液,在20℃下搅拌4小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为1680,式I中m为1.96,n为0.48。3) Dissolve 45 parts by mass of 4,4'-diaminodiphenylmethane in 34 parts by mass of methanol, and after stirring for half an hour, add the above-mentioned NE, the esterification solution of compounds A 2 and B 1 in sequence, and stir at 20°C for 4 hours, a homogeneous polyimide matrix resin solution was obtained, and the calculated number average molecular weight was 1680, m in formula I was 1.96, and n was 0.48.

将步骤3)得到的树脂溶液依次经80℃/3h、150℃/2h、210℃/1h升温热处理,得到树脂模塑粉,测得其最低熔体粘度为120Pa.s;将该模塑粉在250-320℃和3MPa压力下热固化后得到纯树脂模压件,该树脂模压件的玻璃化转变温度大于360℃(采用DMA法测定),拉伸强度大于75MPa,弯曲强度大于130MPa。The resin solution obtained in step 3) is heated and heat-treated at 80°C/3h, 150°C/2h, and 210°C/1h in turn to obtain resin molding powder, and its minimum melt viscosity is measured to be 120Pa.s; the molding powder After thermal curing at 250-320°C and 3MPa pressure, a pure resin molded part can be obtained. The glass transition temperature of the resin molded part is greater than 360°C (measured by DMA method), the tensile strength is greater than 75MPa, and the bending strength is greater than 130MPa.

实施例4、聚酰亚胺树脂的制备以及树脂模压件的性能Embodiment 4, the preparation of polyimide resin and the performance of resin molding

1)将47质量份封端剂降冰片烯二甲酸酐在60质量份乙醇中86℃加热回流5小时得到相应的降冰片烯二甲酸单酯溶液(NE)。1) 47 parts by mass of norbornene dicarboxylic anhydride, an end-capping agent, was heated to reflux at 86° C. for 5 hours in 60 parts by mass of ethanol to obtain the corresponding norbornene dicarboxylic acid monoester solution (NE).

2)将120质量份化合物A2在175质量份乙醇中82℃加热回流6小时得到化合物A2的酯化物溶液,将24质量份化合物B2在30质量份乙醇中83℃加热回流4小时得到化合物B2的酯化物溶液。2) Heat 120 parts by mass of Compound A 2 in 175 parts by mass of ethanol at 82°C for 6 hours to obtain an esterified product solution of Compound A 2 , and heat 24 parts by mass of Compound B 2 in 30 parts by mass of ethanol at 83°C for 4 hours to obtain The esterification product solution of compound B2 .

3)将175质量份1,3-双(4-氨基苯氧基)苯溶解在120质量份乙醇中,搅拌半小时后依次加入NE、化合物A2和B2的酯化物溶液,在40℃下搅拌4小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为2390,式I中m为2.57,n为0.54。3) Dissolve 175 parts by mass of 1,3-bis(4-aminophenoxy)benzene in 120 parts by mass of ethanol, and after stirring for half an hour, add NE, the esterification solution of compounds A 2 and B 2 in sequence, and heat at 40°C Stir for 4 hours to obtain a homogeneous polyimide matrix resin solution, the calculated number average molecular weight is 2390, m in formula I is 2.57, and n is 0.54.

将步骤3)得到的树脂溶液依次经80℃/3h、140℃/2h、220℃/1h升温热处理,得到树脂模塑粉,测得其最低熔体粘度为8Pa.s;将该模塑粉在250-320℃和2MPa压力下热固化后得到纯树脂模压件,该树脂模压件的玻璃化转变温度大于350℃(采用DMA法测定),拉伸强度大于70MPa,弯曲强度大于110MPa。The resin solution obtained in step 3) is heated and heat-treated at 80°C/3h, 140°C/2h, and 220°C/1h to obtain resin molding powder, and its minimum melt viscosity is measured to be 8Pa.s; the molding powder After thermal curing at 250-320°C and 2MPa pressure, a pure resin molded part can be obtained. The glass transition temperature of the resin molded part is greater than 350°C (measured by DMA method), the tensile strength is greater than 70MPa, and the bending strength is greater than 110MPa.

实施例5、聚酰亚胺树脂的制备以及树脂模压件的性能Embodiment 5, the preparation of polyimide resin and the performance of resin molding

1)将15质量份封端剂降冰片烯二甲酸酐在20质量份乙醇中82℃加热回流2小时得到降冰片烯二甲酸单酯溶液(NE)。1) 15 parts by mass of the capping agent norbornene dicarboxylic anhydride was heated to reflux at 82° C. for 2 hours in 20 parts by mass of ethanol to obtain a norbornene dicarboxylic acid monoester solution (NE).

2)将48质量份化合物A3在46质量份甲醇中68℃加热回流4小时得到化合物A3的酯化物溶液,将5质量份化合物B2在5质量份甲醇中69℃加热回流4小时得到化合物B2的酯化物溶液。2) Heat 48 parts by mass of compound A 3 in 46 parts by mass of methanol to reflux at 68°C for 4 hours to obtain an esterification product solution of compound A 3 , and heat 5 parts by mass of compound B 2 to reflux at 69°C in 5 mass parts of methanol for 4 hours to obtain The esterification product solution of compound B2 .

3)将78质量份1,4-双(4-氨基-2-三氟甲基苯氧基)苯溶解在80质量份乙醇中,搅拌半小时后依次加入上述制备的NE、化合物A3和B2的酯化物溶液,在25℃下搅拌9小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为3170,式I中m为2.93,n为0.35。3) Dissolve 78 parts by mass of 1,4-bis(4-amino-2-trifluoromethylphenoxy)benzene in 80 parts by mass of ethanol, stir for half an hour and then add the NE prepared above, compound A 3 and The esterified product solution of B 2 was stirred at 25°C for 9 hours to obtain a homogeneous polyimide matrix resin solution with a calculated number average molecular weight of 3170, m in formula I was 2.93, and n was 0.35.

将步骤3)得到的树脂溶液依次经70℃/3h、140℃/2h、230℃/1h升温热处理,得到树脂模塑粉,测得其最低熔体粘度为28Pa.s;将该模塑粉在250-320℃和1.5MPa压力下热固化后得到纯树脂模压件,该树脂模压件的玻璃化转变温度大于350℃(采用DMA法测定),拉伸强度大于80MPa,弯曲强度大于120MPa。The resin solution obtained in step 3) is heated and heat-treated at 70°C/3h, 140°C/2h, and 230°C/1h in turn to obtain resin molding powder, and its minimum melt viscosity is measured to be 28Pa.s; the molding powder After thermal curing at 250-320°C and 1.5MPa pressure, a pure resin molded part can be obtained. The glass transition temperature of the resin molded part is greater than 350°C (measured by DMA method), the tensile strength is greater than 80MPa, and the bending strength is greater than 120MPa.

实施例6、聚酰亚胺树脂的制备以及树脂模压件的性能Embodiment 6, the preparation of polyimide resin and the performance of resin molding

1)将59质量份封端剂降冰片烯二甲酸酐在62质量份甲醇中67℃加热回流2小时得到相应的降冰片烯二甲酸单酯溶液(NE)。1) 59 parts by mass of the capping agent norbornene dicarboxylic anhydride were heated to reflux at 67° C. for 2 hours in 62 parts by mass of methanol to obtain the corresponding norbornene dicarboxylic acid monoester solution (NE).

2)将193质量份化合物A2在172质量份甲醇中68℃加热回流5小时得到化合物A2的酯化物溶液,将20份化合物B3在18份甲醇中70℃加热回流2小时得到化合物B3的酯化物溶液。2) Heat 193 parts by mass of compound A 2 in 172 parts by mass of methanol at 68°C for 5 hours to obtain an esterification product solution of compound A 2 , and heat 20 parts of compound B 3 in 18 parts of methanol at 70°C for 2 hours to obtain compound B 3 esterification solution.

3)将318质量份4,4’-双(4-氨基-2-三氟甲基苯氧基)联苯溶解在285份甲醇中,搅拌半小时后依次加入上述制备的NE、化合物A2和B3的酯化物溶液,在35℃下搅拌5小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为3640,式I中m为3.29,n为0.25。3) Dissolve 318 parts by mass of 4,4'-bis(4-amino-2-trifluoromethylphenoxy)biphenyl in 285 parts of methanol, and after stirring for half an hour, add the above-prepared NE and compound A 2 and the esterified product solution of B3 , stirred at 35°C for 5 hours to obtain a homogeneous polyimide matrix resin solution, the calculated number average molecular weight was 3640, m in formula I was 3.29, and n was 0.25.

将步骤3)得到的树脂溶液依次经60℃/3h、150℃/2h、230℃/1h升温热处理,得到树脂模塑粉,测得其最低熔体粘度为45Pa.s;将该模塑粉在250-320℃和2MPa压力下热固化后得到纯树脂模压件,该树脂模压件的玻璃化转变温度大于360℃(采用DMA法测定),拉伸强度大于75MPa,弯曲强度大于130MPa。The resin solution obtained in step 3) is heated and heat-treated at 60°C/3h, 150°C/2h, and 230°C/1h in turn to obtain resin molding powder, and its minimum melt viscosity is measured to be 45Pa.s; the molding powder After thermal curing at 250-320°C and 2MPa pressure, a pure resin molded part can be obtained. The glass transition temperature of the resin molded part is greater than 360°C (measured by DMA method), the tensile strength is greater than 75MPa, and the bending strength is greater than 130MPa.

实施例7、聚酰亚胺树脂的制备以及碳纤维聚酰亚胺复合材料层压板的性能Embodiment 7, the preparation of polyimide resin and the performance of carbon fiber polyimide composite laminate

1)将66质量份封端剂降冰片烯二甲酸酐在88质量份乙醇中80℃加热回流6小时得到降冰片烯二甲酸单酯溶液(NE)。1) 66 parts by mass of the capping agent norbornene dicarboxylic anhydride was heated to reflux at 80° C. for 6 hours in 88 parts by mass of ethanol to obtain a norbornene dicarboxylic acid monoester solution (NE).

2)将160质量份化合物A1在225质量份乙醇中81℃加热回流4小时得到化合物A1的酯化物溶液,将18质量份化合物B3在24质量份乙醇中83℃加热回流5小时得到化合物B3的酯化物溶液。2) Heat 160 parts by mass of Compound A 1 in 225 parts by mass of ethanol at 81°C for 4 hours to obtain an esterification product solution of Compound A 1 , and heat 18 parts by mass of Compound B 3 in 24 parts by mass of ethanol at 83°C for 5 hours to obtain The esterification product solution of compound B3 .

3)将54质量份间苯二胺、36份对苯二胺溶解在140质量份乙醇中,搅拌半小时后依次加入上述制备的NE、化合物A1和B3的酯化物溶液,在40℃下搅拌8小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为1500,式I中m为2.71,n为0.20。3) Dissolve 54 parts by mass of m-phenylenediamine and 36 parts of p-phenylenediamine in 140 parts by mass of ethanol, and after stirring for half an hour, add the above-prepared NE, the esterified solution of compounds A 1 and B 3 in sequence, at 40°C Stir for 8 hours to obtain a homogeneous polyimide matrix resin solution, the calculated number average molecular weight is 1500, m in formula I is 2.71, and n is 0.20.

将步骤3)得到的树脂溶液在缠绕机上与碳纤维进行复合制备预浸料,对预浸料进行裁剪、铺层,在50-320℃和4MPa压力下热固化后得到碳纤维聚酰亚胺复合材料层压板。Compound the resin solution obtained in step 3) with carbon fiber on a winding machine to prepare a prepreg, cut and lay up the prepreg, and heat-cure it at 50-320°C and 4MPa pressure to obtain a carbon fiber polyimide composite material laminate.

测得该层压板的玻璃化转变温度大于410℃(采用DMA法测定),弯曲强度大于1500MPa,弯曲模量大于130GPa,层间剪切强度大于60MPa。It is measured that the glass transition temperature of the laminate is greater than 410° C. (measured by DMA method), the bending strength is greater than 1500 MPa, the bending modulus is greater than 130 GPa, and the interlaminar shear strength is greater than 60 MPa.

实施例8、聚酰亚胺树脂的制备以及碳纤维聚酰亚胺复合材料层压板的性能Embodiment 8, the preparation of polyimide resin and the performance of carbon fiber polyimide composite laminate

1)将26质量份封端剂降冰片烯二甲酸酐在33质量份乙醇中84℃加热回流2小时得到相应的降冰片烯二甲酸单酯溶液(NE)。1) 26 parts by mass of the capping agent norbornene dicarboxylic anhydride was heated to reflux at 84° C. for 2 hours in 33 parts by mass of ethanol to obtain the corresponding norbornene dicarboxylic acid monoester solution (NE).

2)将54质量份化合物A1在82质量份乙醇中83℃加热回流6小时得到化合物A1的酯化物溶液,将15质量份化合物B1在21质量份乙醇中82℃加热回流4小时得到化合物B1的酯化物溶液。2) Heat 54 parts by mass of Compound A 1 in 82 parts by mass of ethanol at 83°C for 6 hours to obtain an esterification product solution of Compound A 1 , and heat 15 parts by mass of Compound B 1 in 21 parts by mass of ethanol at 82°C for 4 hours to obtain The esterification product solution of compound B1 .

3)将17质量份对苯二胺、31质量份4,4’-二氨基二苯醚溶解在52质量份乙醇中,搅拌半小时后依次加入上述制备的NE、化合物A1和B1的酯化物溶液,在30℃下搅拌7小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为1660,式I中m为2.32,n为0.59。3) Dissolve 17 parts by mass of p-phenylenediamine and 31 parts by mass of 4,4'-diaminodiphenyl ether in 52 parts by mass of ethanol, and after stirring for half an hour, add the above-prepared NE, compounds A 1 and B 1 in sequence The esterified product solution was stirred at 30°C for 7 hours to obtain a homogeneous polyimide matrix resin solution with a calculated number average molecular weight of 1660, m in formula I being 2.32, and n being 0.59.

将步骤3)得到的树脂溶液在缠绕机上与碳纤维进行复合制备预浸料,对预浸料进行裁剪、铺层,在50-320℃和3MPa压力下热固化后得到碳纤维聚酰亚胺复合材料层压板。Compound the resin solution obtained in step 3) with carbon fiber on a winding machine to prepare a prepreg, cut and lay up the prepreg, and heat-cure at 50-320°C and 3MPa pressure to obtain a carbon fiber polyimide composite material laminate.

测得该层压板的玻璃化转变温度大于400℃(采用DMA法测定),弯曲强度大于1500MPa,弯曲模量大于110GPa,层间剪切强度大于75MPa。It is measured that the glass transition temperature of the laminate is greater than 400°C (measured by DMA method), the bending strength is greater than 1500MPa, the bending modulus is greater than 110GPa, and the interlaminar shear strength is greater than 75MPa.

实施例9、聚酰亚胺树脂的制备以及树脂模压件的性能Embodiment 9, the preparation of polyimide resin and the performance of resin molding

1)将18质量份封端剂降冰片烯二甲酸酐在20质量份甲醇中70℃加热回流1小时得到降冰片烯二甲酸单酯溶液(NE)。1) 18 parts by mass of the capping agent norbornene dicarboxylic anhydride was heated to reflux at 70° C. for 1 hour in 20 parts by mass of methanol to obtain a norbornene dicarboxylic acid monoester solution (NE).

2)将34质量份化合物A1在39质量份甲醇中68℃加热回流4小时得到化合物A1的酯化物溶液,将7质量份化合物B2在8质量份甲醇中67℃加热回流3小时得到化合物B2的酯化物溶液。2) Heat 34 parts by mass of compound A 1 in 39 parts by mass of methanol to reflux at 68°C for 4 hours to obtain an esterification product solution of compound A 1 , and heat 7 parts by mass of compound B 2 to reflux at 67°C in 8 mass parts of methanol for 3 hours to obtain The esterification product solution of compound B2 .

3)将30质量份4,4’-二氨基二苯醚、15质量份4,4’-二氨基二苯甲烷溶解在34份甲醇中,搅拌半小时后依次加入上述制备的NE、化合物A1和B2的酯化物溶液,在40℃下搅拌10小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为1650,式I中m为2.11,n为0.41。3) Dissolve 30 parts by mass of 4,4'-diaminodiphenyl ether and 15 parts by mass of 4,4'-diaminodiphenylmethane in 34 parts of methanol, stir for half an hour and then add the above-prepared NE and compound A in sequence The esterified product solution of 1 and B 2 was stirred at 40°C for 10 hours to obtain a homogeneous polyimide matrix resin solution, the calculated number average molecular weight was 1650, m in formula I was 2.11, and n was 0.41.

将步骤3)得到的树脂溶液依次经70℃/3h、140℃/2h、220℃/1h升温热处理,得到树脂模塑粉,测得其最低熔体粘度为110Pa.s;将该模塑粉在250-320℃和3MPa压力下热固化后得到纯树脂模压件,该树脂模压件的玻璃化转变温度大于370℃(采用DMA法测定),拉伸强度大于75MPa,弯曲强度大于130MPa。The resin solution obtained in step 3) is heated and heat-treated at 70°C/3h, 140°C/2h, and 220°C/1h in turn to obtain resin molding powder, and its minimum melt viscosity is measured to be 110Pa.s; the molding powder After thermal curing at 250-320°C and 3MPa pressure, a pure resin molded part can be obtained. The glass transition temperature of the resin molded part is greater than 370°C (measured by DMA method), the tensile strength is greater than 75MPa, and the bending strength is greater than 130MPa.

实施例10、聚酰亚胺树脂的制备以及树脂模压件的性能Embodiment 10, the preparation of polyimide resin and the performance of resin molding

1)将24质量份封端剂降冰片烯二甲酸酐在33质量份乙醇中85℃加热回流6小时得到相应的降冰片烯二甲酸单酯溶液(NE)。1) 24 parts by mass of the capping agent norbornene dicarboxylic anhydride was heated to reflux at 85° C. for 6 hours in 33 parts by mass of ethanol to obtain the corresponding norbornene dicarboxylic acid monoester solution (NE).

2)将63质量份化合物A2在86质量份乙醇中83℃加热回流3小时得到化合物A2的酯化物溶液,将6质量份化合物B3在9质量份乙醇中86℃加热回流5小时得到化合物B3的酯化物溶液。2) Heat 63 parts by mass of Compound A 2 in 86 parts by mass of ethanol at 83°C to reflux for 3 hours to obtain an esterified product solution of Compound A 2 , and heat 6 parts by mass of Compound B 3 in 9 parts by mass of ethanol to reflux at 86°C for 5 hours to obtain The esterification product solution of compound B3 .

3)将16质量份间苯二胺、32质量份1,4-双(4-氨基-2-三氟甲基苯氧基)苯、15质量份3,4’-二氨基二苯醚溶解在60质量份乙醇中,搅拌半小时后依次加入上述制备的NE、化合物A2和B3的酯化物溶液,在20℃下搅拌3小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为1940,式I中m为2.64,n为0.18。3) Dissolve 16 parts by mass of m-phenylenediamine, 32 parts by mass of 1,4-bis(4-amino-2-trifluoromethylphenoxy)benzene, and 15 parts by mass of 3,4'-diaminodiphenyl ether In 60 parts by mass of ethanol, after stirring for half an hour, add the esterified solution of NE, compound A 2 and B 3 prepared above in sequence, and stir at 20°C for 3 hours to obtain a homogeneous polyimide matrix resin solution, and calculate the number average The molecular weight is 1940, and m is 2.64 in formula I, and n is 0.18.

将步骤3)得到的树脂溶液依次经70℃/3h、150℃/2h、210℃/1h升温热处理,得到树脂模塑粉,测得其最低熔体粘度为50Pa.s;将该模塑粉在250-320℃和4MPa压力下热固化后得到纯树脂模压件,该树脂模压件的玻璃化转变温度大于360℃(采用DMA法测定),拉伸强度大于70MPa,弯曲强度大于120MPa。The resin solution obtained in step 3) is heated and heat-treated at 70°C/3h, 150°C/2h, and 210°C/1h in turn to obtain resin molding powder, and its minimum melt viscosity is measured to be 50Pa.s; the molding powder After thermal curing at 250-320°C and 4MPa pressure, a pure resin molded part can be obtained. The glass transition temperature of the resin molded part is greater than 360°C (measured by DMA method), the tensile strength is greater than 70MPa, and the bending strength is greater than 120MPa.

实施例11、聚酰亚胺树脂的制备以及树脂模压件的性能Embodiment 11, the preparation of polyimide resin and the performance of resin molding

1)将21质量份封端剂降冰片烯二甲酸酐在28质量份乙醇中81℃加热回流3小时得到相应的降冰片烯二甲酸单酯溶液(NE)。1) 21 parts by mass of the capping agent norbornene dicarboxylic anhydride was heated to reflux at 81° C. for 3 hours in 28 parts by mass of ethanol to obtain the corresponding norbornene dicarboxylic acid monoester solution (NE).

2)将48质量份化合物A1在70质量份乙醇中84℃加热回流4小时得到化合物A1的酯化物溶液,将9质量份化合物B1在12质量份乙醇中82℃加热回流3小时得到化合物B1的酯化物溶液。2) Heat 48 parts by mass of Compound A 1 in 70 parts by mass of ethanol at 84°C for 4 hours to obtain an esterified product solution of Compound A 1 , and heat 9 parts by mass of Compound B 1 in 12 parts by mass of ethanol at 82°C for 3 hours to obtain The esterification product solution of compound B1 .

3)将39份1,3-双(4-氨基苯氧基)苯、13份3,4’-二氨基二苯醚、19份1,4-双(4-氨基苯氧基)苯溶解在60份乙醇和15份丙酮的混合溶剂中,搅拌半小时后依次加入上述制备的NE、化合物A1和B1的酯化物溶液,在35℃下搅拌7小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为2150,式I中m为2.55,n为0.44。3) Dissolve 39 parts of 1,3-bis(4-aminophenoxy)benzene, 13 parts of 3,4'-diaminodiphenyl ether, and 19 parts of 1,4-bis(4-aminophenoxy)benzene In a mixed solvent of 60 parts of ethanol and 15 parts of acetone, after stirring for half an hour, add the above-prepared NE, compound A 1 and the esterification solution of B 1 in sequence, and stir at 35°C for 7 hours to obtain a homogeneous polyimide matrix The resin solution has a calculated number average molecular weight of 2150, m in formula I is 2.55, and n is 0.44.

将步骤3)得到的树脂溶液依次经80℃/3h、140℃/2h、200℃/1h升温热处理,得到树脂模塑粉,测得其最低熔体粘度为75Pa.s;将该模塑粉在250-320℃和2MPa压力下热固化后得到纯树脂模压件,该树脂模压件的玻璃化转变温度大于350℃(采用DMA法测定),拉伸强度大于75MPa,弯曲强度大于120MPa。The resin solution obtained in step 3) is heated and heat-treated at 80°C/3h, 140°C/2h, and 200°C/1h in turn to obtain resin molding powder, and its minimum melt viscosity is measured to be 75Pa.s; the molding powder After thermal curing at 250-320°C and 2MPa pressure, a pure resin molded part can be obtained. The glass transition temperature of the resin molded part is greater than 350°C (measured by DMA method), the tensile strength is greater than 75MPa, and the bending strength is greater than 120MPa.

实施例12、聚酰亚胺树脂的制备以及碳纤维聚酰亚胺复合材料层压板的性能Example 12, preparation of polyimide resin and performance of carbon fiber polyimide composite laminate

1)将14质量份封端剂降冰片烯二甲酸酐在18质量份乙醇中86℃加热回流4小时得到相应的降冰片烯二甲酸单酯溶液(NE)。1) 14 parts by mass of end-capping agent norbornene dicarboxylic anhydride was heated to reflux at 86° C. for 4 hours in 18 parts by mass of ethanol to obtain the corresponding norbornene dicarboxylic acid monoester solution (NE).

2)将42质量份化合物A3在53质量份乙醇中82℃加热回流3小时得到化合物A3的酯化物溶液,将4质量份化合物B3在6质量份乙醇中83℃加热回流2小时得到化合物B3的酯化物溶液。2) Heat 42 parts by mass of compound A 3 in 53 parts by mass of ethanol at 82°C to reflux for 3 hours to obtain an esterified product solution of compound A 3 , and heat 4 mass parts of compound B 3 in 6 mass parts of ethanol to reflux at 83°C for 2 hours to obtain The esterification product solution of compound B3 .

3)将6质量份对苯二胺、11质量份4,4’-二氨基二苯甲烷、24质量份4,4’-双(4-氨基-2-三氟甲基苯氧基)联苯溶解在32质量份乙醇中,搅拌半小时后依次加入上述制备的NE、化合物A3和B3的酯化物溶液,在40℃下搅拌9小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为2290,式I中m为2.75,n为0.21。3) 6 parts by mass of p-phenylenediamine, 11 parts by mass of 4,4'-diaminodiphenylmethane, 24 parts by mass of 4,4'-bis(4-amino-2-trifluoromethylphenoxy) Benzene was dissolved in 32 parts by mass of ethanol, and after stirring for half an hour, the esterified solution of NE, compound A3 and B3 prepared above was added in sequence, and stirred at 40°C for 9 hours to obtain a homogeneous polyimide matrix resin solution, calculated The number average molecular weight is 2290, m is 2.75 in formula I, and n is 0.21.

将步骤3)得到的树脂溶液在缠绕机上与碳纤维进行复合制备预浸料,对预浸料进行裁剪、铺层,在50-320℃和3MPa压力下热固化后得到碳纤维聚酰亚胺复合材料层压板。Compound the resin solution obtained in step 3) with carbon fiber on a winding machine to prepare a prepreg, cut and lay up the prepreg, and heat-cure at 50-320°C and 3MPa pressure to obtain a carbon fiber polyimide composite material laminate.

测得该层压板的玻璃化转变温度大于370℃(采用DMA法测定),弯曲强度大于1300MPa,弯曲模量大于90GPa,层间剪切强度大于70MPa。It is measured that the glass transition temperature of the laminate is greater than 370°C (measured by DMA method), the bending strength is greater than 1300MPa, the bending modulus is greater than 90GPa, and the interlaminar shear strength is greater than 70MPa.

实施例13、聚酰亚胺树脂的制备以及树脂模压件的性能Example 13, preparation of polyimide resin and properties of resin molded parts

1)将44质量份封端剂降冰片烯二甲酸酐在45质量份甲醇中68℃加热回流1小时得到降冰片烯二甲酸单酯溶液(NE)。1) 44 parts by mass of the capping agent norbornene dicarboxylic anhydride was heated to reflux at 68° C. for 1 hour in 45 parts by mass of methanol to obtain a norbornene dicarboxylic acid monoester solution (NE).

2)将100质量份化合物A1在105质量份甲醇中69℃加热回流4小时得到化合物A1的酯化物溶液,将1质量份化合物B2在1质量份甲醇中67℃加热回流3小时得到化合物B2的酯化物溶液。2) Heat 100 parts by mass of compound A 1 in 105 parts by mass of methanol to reflux at 69°C for 4 hours to obtain an esterification solution of compound A 1 , and heat 1 mass part of compound B 2 in 1 mass part of methanol to reflux at 67°C for 3 hours to obtain The esterification product solution of compound B2 .

3)将149质量份2,2’-二三氟甲基-4,4’-二氨基联苯溶解在130份乙醇中,搅拌半小时后依次加入上述制备的NE、化合物A1和B2的酯化物溶液,在35℃下搅拌8小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为2080,式I中m为2.54,n为0.02。3) Dissolve 149 parts by mass of 2,2'-bistrifluoromethyl-4,4'-diaminobiphenyl in 130 parts of ethanol, stir for half an hour and then add the above-prepared NE, compounds A 1 and B 2 in sequence The esterified product solution was stirred at 35°C for 8 hours to obtain a homogeneous polyimide matrix resin solution, the calculated number average molecular weight was 2080, m in formula I was 2.54, and n was 0.02.

将步骤3)得到的树脂溶液依次经60℃/3h、140℃/2h、220℃/1h升温热处理,得到树脂模塑粉,测得其最低熔体粘度为130Pa.s;将该模塑粉在250-320℃和3MPa压力下热固化后得到纯树脂模压件,该树脂模压件的玻璃化转变温度大于360℃(采用DMA法测定),拉伸强度大于70MPa,弯曲强度大于120MPa。The resin solution obtained in step 3) is heated and heat-treated at 60°C/3h, 140°C/2h, and 220°C/1h in turn to obtain resin molding powder, and its minimum melt viscosity is measured to be 130Pa.s; the molding powder After thermal curing at 250-320°C and 3MPa pressure, a pure resin molded part can be obtained. The glass transition temperature of the resin molded part is greater than 360°C (measured by DMA method), the tensile strength is greater than 70MPa, and the bending strength is greater than 120MPa.

实施例14、聚酰亚胺树脂的制备以及树脂模压件的性能Example 14, Preparation of polyimide resin and properties of resin molded parts

1)将5质量份封端剂降冰片烯二甲酸酐在6质量份甲醇中69℃加热回流3小时得到降冰片烯二甲酸单酯溶液(NE)。1) 5 parts by mass of end-capping agent norbornene dicarboxylic anhydride was heated to reflux at 69° C. for 3 hours in 6 parts by mass of methanol to obtain norbornene dicarboxylic acid monoester solution (NE).

2)将80质量份化合物A1在78质量份甲醇中67℃加热回流5小时得到化合物A1的酯化物溶液,将20质量份化合物B3在25质量份甲醇中68℃加热回流4小时得到化合物B3的酯化物溶液。2) Heat 80 parts by mass of compound A 1 in 78 parts by mass of methanol to reflux at 67°C for 5 hours to obtain an esterified product solution of compound A 1 , and heat 20 parts by mass of compound B 3 to reflux at 68°C in 25 parts by mass of methanol for 4 hours to obtain The esterification product solution of compound B3 .

3)将24质量份间苯二胺,23质量份3,4’-二氨基二苯醚溶解在45份甲醇中,搅拌半小时后依次加入上述制备的NE、化合物A1和B3的酯化物溶液,在30℃下搅拌8小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为8950,式I中m为17.85,n为2.95。3) Dissolve 24 parts by mass of m-phenylenediamine and 23 parts by mass of 3,4'-diaminodiphenyl ether in 45 parts of methanol, and after stirring for half an hour, add the esters of NE, compounds A 1 and B 3 prepared above in sequence The compound solution was stirred at 30°C for 8 hours to obtain a homogeneous polyimide matrix resin solution, the calculated number average molecular weight was 8950, m in formula I was 17.85, and n was 2.95.

将步骤3)得到的树脂溶液依次经60℃/3h、150℃/2h、200℃/1h升温热处理,得到树脂模塑粉,测得其最低熔体粘度为2300Pa.s;将该模塑粉在250-320℃和3MPa压力下热固化后得到纯树脂模压件,该树脂模压件的玻璃化转变温度大于350℃(采用DMA法测定),拉伸强度大于80MPa,弯曲强度大于120MPa。The resin solution obtained in step 3) is heated and heat-treated at 60°C/3h, 150°C/2h, and 200°C/1h in turn to obtain resin molding powder, and its minimum melt viscosity is measured to be 2300Pa.s; the molding powder After thermal curing at 250-320°C and 3MPa pressure, a pure resin molded part can be obtained. The glass transition temperature of the resin molded part is greater than 350°C (measured by DMA method), the tensile strength is greater than 80MPa, and the bending strength is greater than 120MPa.

实施例15、聚酰亚胺树脂的制备以及树脂模压件的性能Example 15, Preparation of polyimide resin and properties of resin molded parts

1)将80质量份封端剂降冰片烯二甲酸酐在110质量份乙醇中83℃加热回流3小时得到降冰片烯二甲酸单酯溶液(NE)。1) 80 parts by mass of the capping agent norbornene dicarboxylic anhydride was heated to reflux at 83° C. for 3 hours in 110 parts by mass of ethanol to obtain a norbornene dicarboxylic acid monoester solution (NE).

2)将95质量份化合物A1在125质量份乙醇中85℃加热回流4小时得到化合物A1的酯化物溶液,将5质量份化合物B2在8质量份乙醇中82℃加热回流4小时得到化合物B2的酯化物溶液。2) Heat 95 parts by mass of compound A 1 in 125 parts by mass of ethanol at 85°C for 4 hours to obtain an esterification product solution of compound A 1 , and heat 5 parts by mass of compound B 2 in 8 mass parts of ethanol at 82°C for 4 hours to obtain The esterification product solution of compound B2 .

3)将55质量份4,4’-二氨基二苯醚,55质量份3,4’-二氨基二苯醚溶解在105份乙醇中,搅拌半小时后依次加入上述制备的NE、化合物A1和B2的酯化物溶液,在25℃下搅拌6小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为1130,式I中m为1.33,n为0.07。3) Dissolve 55 parts by mass of 4,4'-diaminodiphenyl ether and 55 parts by mass of 3,4'-diaminodiphenyl ether in 105 parts of ethanol, stir for half an hour and then add the above-prepared NE and compound A in sequence The esterified solution of 1 and B 2 was stirred at 25°C for 6 hours to obtain a homogeneous polyimide matrix resin solution with a calculated number average molecular weight of 1130, m in formula I was 1.33, and n was 0.07.

将步骤3)得到的树脂溶液依次经80℃/3h、140℃/2h、200℃/1h升温热处理,得到树脂模塑粉,测得其最低熔体粘度为45Pa.s;将该模塑粉在250-320℃和2MPa压力下热固化后得到纯树脂模压件,该树脂模压件的玻璃化转变温度大于360℃(采用DMA法测定),拉伸强度大于50MPa,弯曲强度大于110MPa。The resin solution obtained in step 3) is heated and heat-treated at 80°C/3h, 140°C/2h, and 200°C/1h to obtain resin molding powder, and its minimum melt viscosity is measured to be 45Pa.s; the molding powder After thermal curing at 250-320°C and 2MPa pressure, a pure resin molded part can be obtained. The glass transition temperature of the resin molded part is greater than 360°C (measured by DMA method), the tensile strength is greater than 50MPa, and the bending strength is greater than 110MPa.

实施例16、聚酰亚胺树脂的制备以及树脂模压件的性能Example 16, Preparation of polyimide resin and properties of resin molded parts

1)将24质量份封端剂降冰片烯二甲酸酐在20质量份甲醇中69℃加热回流3小时得到降冰片烯二甲酸单酯溶液(NE)。1) 24 parts by mass of end-capping agent norbornene dicarboxylic anhydride was heated to reflux at 69° C. for 3 hours in 20 parts by mass of methanol to obtain norbornene dicarboxylic acid monoester solution (NE).

2)将75质量份化合物A2在85质量份甲醇中68℃加热回流4小时得到化合物A2的酯化物溶液,将25质量份化合物B3在26质量份甲醇中68℃加热回流4小时得到化合物B3的酯化物溶液。2) Heat 75 parts by mass of Compound A 2 in 85 parts by mass of methanol to reflux at 68°C for 4 hours to obtain an esterified product solution of Compound A 2 , and heat 25 parts by mass of Compound B 3 to reflux at 68°C in 26 parts by mass of methanol for 4 hours to obtain The esterification product solution of compound B3 .

3)将20质量份间苯二胺,10质量份3,4’-二氨基二苯醚溶解在35份甲醇中,搅拌半小时后依次加入上述制备的NE、化合物A2和B3的酯化物溶液,在20℃下搅拌6小时,得到均相聚酰亚胺基体树脂溶液,计算数均分子量为2150,式I中m为3.15,n为0.77。3) Dissolve 20 parts by mass of m-phenylenediamine and 10 parts by mass of 3,4'-diaminodiphenyl ether in 35 parts of methanol, and after stirring for half an hour, add the esters of NE, compounds A 2 and B 3 prepared above in sequence The compound solution was stirred at 20°C for 6 hours to obtain a homogeneous polyimide matrix resin solution, the calculated number average molecular weight was 2150, m in formula I was 3.15, and n was 0.77.

将步骤3)得到的树脂溶液依次经60℃/3h、140℃/2h、200℃/Ih升温热处理,得到树脂模塑粉,测得其最低熔体粘度为170Pa.s;将该模塑粉在250-320℃和2MPa压力下热固化后得到纯树脂模压件,该树脂模压件的玻璃化转变温度大于350℃(采用DMA法测定),拉伸强度大于60MPa,弯曲强度大于110MPa。The resin solution obtained in step 3) is successively heated and heat-treated at 60°C/3h, 140°C/2h, and 200°C/1h to obtain a resin molding powder, and its minimum melt viscosity is measured to be 170Pa.s; the molding powder After thermal curing at 250-320°C and 2MPa pressure, a pure resin molded part can be obtained. The glass transition temperature of the resin molded part is greater than 350°C (measured by DMA method), the tensile strength is greater than 60MPa, and the bending strength is greater than 110MPa.

Claims (10)

1.结构通式如式I所示的聚酰亚胺树脂,1. general structural formula is as the polyimide resin shown in formula I,
Figure F2009100939220C00011
Figure F2009100939220C00011
(式I)(Formula I) 式I中,In formula I,
Figure F2009100939220C00012
Figure F2009100939220C00012
Figure F2009100939220C00013
Figure F2009100939220C00013
R2= 
Figure DEST_PATH_FSB00000359042200011
-O-,或 
Figure DEST_PATH_FSB00000359042200012
R 2 =
Figure DEST_PATH_FSB00000359042200011
-O-, or
Figure DEST_PATH_FSB00000359042200012
所述m=1-20,n=0.01-6。Said m=1-20, n=0.01-6.
2.根据权利要求1所述的聚酰亚胺树脂,其特征在于:所述聚酰亚胺树脂的数均分子量为1000-9000。2. The polyimide resin according to claim 1, characterized in that: the number average molecular weight of the polyimide resin is 1000-9000. 3.一种制备权利要求1所述式I所示的聚酰亚胺树脂的方法,包括以下步骤:3. a method for preparing the polyimide resin shown in formula I described in claim 1, comprises the following steps: 1)将封端剂与有机脂肪醇溶剂进行酯化反应,得到封端剂单酸单酯溶液;1) Esterifying the end-capping agent with an organic aliphatic alcohol solvent to obtain a monoacid monoester solution of the end-capping agent; 2)将芳香族四酸二酐与有机脂肪醇溶剂进行酯化反应,得到芳香族四酸二酯溶液;2) Esterifying the aromatic tetra-acid dianhydride with an organic aliphatic alcohol solvent to obtain an aromatic tetra-acid diester solution; 3)将芳香族二胺溶解于有机脂肪醇溶剂中,然后依次加入步骤1)的封端剂单酸单酯溶液、步骤2)的芳香族四酸二酯溶液进行反应,得到式I所示的聚酰亚胺树脂溶液;3) dissolving the aromatic diamine in an organic aliphatic alcohol solvent, then adding the end-capping agent monoacid monoester solution in step 1) and the aromatic tetraacid diester solution in step 2) to react to obtain the formula shown in I The polyimide resin solution; 其中,所述封端剂为式II所示的化合物,Wherein, the capping agent is a compound shown in formula II, (式II);(Formula II); 所述芳香族四酸二酐为下述芳香族四酸二酐I与芳香族四酸二酐II的混合物,其中,芳香族四酸二酐I与芳香族四酸二酐II的质量份数比为100∶1-30;The aromatic tetra-acid dianhydride is a mixture of the following aromatic tetra-acid dianhydride I and aromatic tetra-acid dianhydride II, wherein the mass fraction of aromatic tetra-acid dianhydride I and aromatic tetra-acid dianhydride II The ratio is 100:1-30; 所述芳香族四酸二酐I选自下述式A1、式A2、式A3所示化合物中的一种:The aromatic tetra-acid dianhydride I is selected from one of the compounds shown in the following formula A1, formula A2, and formula A3: 式A1    式A2    式A3Type A1 Type A2 Type A3 所述芳香族四酸二酐II选自下述式B1、式B2、式B3所示化合物中的一种:The aromatic tetra-acid dianhydride II is selected from one of the compounds shown in the following formula B1, formula B2, and formula B3:
Figure RE-FSB00000359042200015
Figure RE-FSB00000359042200015
式B1    式B2    式B3Formula B1 Formula B2 Formula B3 所述芳香族二胺选自下述化合物中的一种: The aromatic diamine is selected from one of the following compounds:
Figure RE-FSB00000359042200021
Figure RE-FSB00000359042200021
所述封端剂、芳香族四酸二酐和芳香族二胺的质量份数比依次为5-80∶100∶30-150。The ratio of the number of parts by mass of the end-capping agent, aromatic tetra-acid dianhydride and aromatic diamine is 5-80:100:30-150 in sequence.
4.根据权利要求3所述的方法,其特征在于:步骤3)中所述反应的反应温度为5-40℃,反应时间为1-10小时。4. The method according to claim 3, characterized in that: the reaction temperature of the reaction in step 3) is 5-40° C., and the reaction time is 1-10 hours. 5.根据权利要求3或4所述的方法,其特征在于:步骤1)、步骤2)和步骤3)中所述有机脂肪醇溶剂为下述醇中的至少一种:甲醇、乙醇、丙醇、异丙醇、正丁醇、异丁醇、正戊醇、异戊醇和叔丁醇;或为上述醇中的一种与下述至少一种溶剂的任意比例混合的混合物:丙酮、四氢呋喃、二氧六环、苯、甲苯、氯仿和二氯甲烷。5. according to the described method of claim 3 or 4, it is characterized in that: organic fatty alcohol solvent described in step 1), step 2) and step 3) is at least one in following alcohol: methyl alcohol, ethanol, propane Alcohol, isopropanol, n-butanol, isobutanol, n-pentanol, isoamyl alcohol, and tert-butanol; or a mixture of any of the above alcohols in any proportion with at least one of the following solvents: acetone, tetrahydrofuran , dioxane, benzene, toluene, chloroform and dichloromethane. 6.根据权利要求3所述的方法,其特征在于:步骤1)中所述封端剂与有机脂肪醇溶剂的质量份数比为5-60∶5-600;步骤1)中所述酯化反应在65-140℃加热 回流的条件下进行,反应时间为1-6小时。6. The method according to claim 3, characterized in that: the mass and number ratio of the capping agent and the organic fatty alcohol solvent in step 1) is 5-60: 5-600; the ester described in step 1) The reaction is carried out under the condition of heating and reflux at 65-140° C., and the reaction time is 1-6 hours. 7.根据权利要求3所述的方法,其特征在于:步骤2)中所述芳香族四酸二酐与有机脂肪醇溶剂的质量份数比为100∶60-1200;步骤2)中所述酯化反应在65-140℃加热回流的条件下进行,反应时间为1-6小时。7. The method according to claim 3, characterized in that: the mass fraction ratio of aromatic tetraacid dianhydride and organic aliphatic alcohol solvent described in step 2) is 100: 60-1200; described in step 2) The esterification reaction is carried out under the condition of heating and refluxing at 65-140° C., and the reaction time is 1-6 hours. 8.根据权利要求3所述的方法,其特征在于:步骤3)中所述芳香族二胺与有机脂肪醇溶剂的质量份数比为30-150∶10-800。8. The method according to claim 3, characterized in that: in step 3), the ratio of aromatic diamine to organic aliphatic alcohol solvent in parts by mass is 30-150:10-800. 9.根据权利要求3所述的方法,其特征在于:所述方法还包括对步骤3)得到的聚酰亚胺树脂溶液进行热处理,得到固态聚酰亚胺树脂的步骤。9. The method according to claim 3, characterized in that: said method further comprises the step of heat-treating the polyimide resin solution obtained in step 3) to obtain a solid polyimide resin. 10.权利要求1所述式I所示的聚酰亚胺树脂在制备聚酰亚胺树脂基复合材料中的应用。 10. the application of polyimide resin shown in formula I described in claim 1 in the preparation polyimide resin-based composite material. the
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