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CN106866964A - A kind of polyimide foam and preparation method thereof - Google Patents

A kind of polyimide foam and preparation method thereof Download PDF

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CN106866964A
CN106866964A CN201510925204.0A CN201510925204A CN106866964A CN 106866964 A CN106866964 A CN 106866964A CN 201510925204 A CN201510925204 A CN 201510925204A CN 106866964 A CN106866964 A CN 106866964A
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aromatic
preparation
dianhydride
foam
precursor solution
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郭宝华
丁光敏
徐军
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Tsinghua University
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G73/00Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
    • C08G73/06Polycondensates having nitrogen-containing heterocyclic rings in the main chain of the macromolecule
    • C08G73/10Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
    • C08G73/1067Wholly aromatic polyimides, i.e. having both tetracarboxylic and diamino moieties aromatically bound
    • C08G73/1071Wholly aromatic polyimides containing oxygen in the form of ether bonds in the main chain
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G73/00Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
    • C08G73/06Polycondensates having nitrogen-containing heterocyclic rings in the main chain of the macromolecule
    • C08G73/10Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
    • C08G73/1067Wholly aromatic polyimides, i.e. having both tetracarboxylic and diamino moieties aromatically bound
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/28Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof by elimination of a liquid phase from a macromolecular composition or article, e.g. drying of coagulum
    • C08J9/286Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof by elimination of a liquid phase from a macromolecular composition or article, e.g. drying of coagulum the liquid phase being a solvent for the monomers but not for the resulting macromolecular composition, i.e. macroporous or macroreticular polymers

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)

Abstract

本发明涉及一种聚酰亚胺泡沫塑料的制备方法,包括以下步骤:(1)在反应器中加入芳香二胺及低分子醇与四氢呋喃的混合溶剂,均匀搅拌后加入芳香二酐进行反应;(2)在步骤(1)得到的反应溶液中加入芳香四酸,使芳香四酸的加入量以(芳香二酐+芳香四酸):芳香二胺的摩尔比为1:1,并继续进行反应得到聚酰亚胺前驱体溶液;(3)将步骤(2)得到的前驱体溶液干燥、粉碎成粉末后铺入模具中升温发泡得到最终的聚酰亚胺泡沫塑料。本发明的制备方法中,通过将部分芳香二酐与适当比例的芳香四酸置换,获得低本体粘度前驱体溶液同时又保持泡沫最终性能。同时保证了材料的发泡温度跟传统工艺相匹配。

The invention relates to a preparation method of polyimide foam plastics, comprising the following steps: (1) adding aromatic diamine, a mixed solvent of low-molecular alcohol and tetrahydrofuran into a reactor, stirring evenly, adding aromatic dianhydride to react; (2) Add aromatic tetraacid to the reaction solution obtained in step (1), so that the amount of aromatic tetraacid added is (aromatic dianhydride+aromatic tetraacid): the molar ratio of aromatic diamine is 1:1, and continue Reaction to obtain a polyimide precursor solution; (3) drying the precursor solution obtained in step (2), pulverizing it into powder, spreading it into a mold, raising the temperature and foaming to obtain the final polyimide foam plastic. In the preparation method of the present invention, by substituting part of the aromatic dianhydride with an appropriate proportion of aromatic tetraacid, a precursor solution with low bulk viscosity is obtained while maintaining the final performance of the foam. At the same time, it ensures that the foaming temperature of the material matches the traditional process.

Description

一种聚酰亚胺泡沫塑料及其制备方法A kind of polyimide foam plastics and preparation method thereof

技术领域technical field

本发明属于高分子材料技术领域,具体涉及一种聚酰亚胺泡沫塑料及其制备方法。The invention belongs to the technical field of polymer materials, and in particular relates to a polyimide foam plastic and a preparation method thereof.

背景技术Background technique

聚酰亚胺泡沫塑料由于其优异的综合性能成为近年来各国研究热点之一。聚酰亚胺泡沫塑料具有耐温性好(-250℃~450℃)、阻燃隔热性能优良、抗辐射、毒性低、耐氧化、耐水解、吸声性能优良等诸多特性。可广泛用于军工及航天业如火箭、飞机隔热、航母、潜艇等隔热吸声方面,以及民用耐高温隔热降噪领域。然而能用来合成高性能聚酰亚胺泡沫的原料种类较少、价格高、且对原料纯度要求高、合成体系粘度大,对该材料的广泛应用带来阻力。Due to its excellent comprehensive performance, polyimide foam has become one of the research hotspots in various countries in recent years. Polyimide foam has many characteristics such as good temperature resistance (-250°C ~ 450°C), excellent flame retardant and heat insulation properties, radiation resistance, low toxicity, oxidation resistance, hydrolysis resistance, and excellent sound absorption performance. It can be widely used in military and aerospace industries such as heat insulation of rockets, aircraft, aircraft carriers, submarines, etc., as well as in the field of high temperature resistance, heat insulation and noise reduction for civilian use. However, there are few types of raw materials that can be used to synthesize high-performance polyimide foam, the price is high, and the requirements for the purity of raw materials are high, and the viscosity of the synthesis system is high, which brings resistance to the wide application of this material.

聚酰亚胺泡沫塑料的研究始于二十世纪60年代,当时美国的Dupont公司申请了聚酰亚胺泡沫的相关专利US3249561,该专利使用了可产生气体的酸并制成一层湿膜或者注射进模腔高温固化成型,制备泡沫密度在40Kg/m3左右的泡沫。后续出现了大量关于聚酰亚胺泡沫的研究,在制备工艺上也趋于多元化,CN103012793采用酯化法将反应完的聚酯胺盐前驱体溶液磨成粉后先通过微波方式发成低密度的聚酰亚胺泡沫方胚,再将其压制成不同密度的聚酰亚胺泡沫板。US8765830使用两至三种的芳香二酐及芳香二胺,通过特定比例合成泡沫均匀、性能优良的聚酰亚胺泡沫。CN102850569借由二酐酯化后与二胺混合得到发泡前体之后,加入酰胺、羧酸、酮等数种添加剂,增加了聚合物分子链的相对移动性,使得聚酰亚胺最终的分子量得以提高,提高了性能。The research on polyimide foam plastics began in the 1960s. At that time, the Dupont Company of the United States applied for the related patent US3249561 of polyimide foam. This patent used an acid that can generate gas and made a wet film or Injected into the mold cavity and cured at high temperature to prepare a foam with a foam density of about 40Kg/m 3 . Subsequent researches on polyimide foam have appeared in a large number, and the preparation process also tends to be diversified. CN103012793 adopts the esterification method to grind the reacted polyester amine salt precursor solution into powder, and then sends it into low-grade polyimide foam by microwave. Density of polyimide foam billets, and then pressed into polyimide foam boards of different densities. US8765830 uses two to three aromatic dianhydrides and aromatic diamines to synthesize a polyimide foam with uniform foam and excellent performance through a specific ratio. CN102850569 After the foaming precursor is obtained by mixing the dianhydride with the diamine after esterification, several additives such as amides, carboxylic acids, and ketones are added to increase the relative mobility of the polymer molecular chain, so that the final molecular weight of the polyimide Can be improved to improve performance.

上述专利中,大部分皆使用了酯化法两步反应得到聚酰亚胺前驱体溶液,并精细的调配原料比例或是外加添加剂提高聚酰亚胺泡沫的性能,且工艺制备较为繁杂。而较高粘度的前驱体意味着难以粉碎成均匀粉末,不易制备孔径均匀的聚酰亚胺泡沫塑料。将部分二酐改为用四酸加入是制备聚酰亚胺材料时降低前驱体溶液粘度采用的方法之一,然而在泡沫领域基本没有报道。本发明通过合理调控四酸及二酐的种类及比例并一步升温完成发泡及酰亚胺化,制备出一系列性能优异的聚酰亚胺泡沫塑料。Most of the above-mentioned patents use the two-step reaction of the esterification method to obtain the polyimide precursor solution, and finely adjust the ratio of raw materials or add additives to improve the performance of the polyimide foam, and the process preparation is relatively complicated. The higher viscosity precursor means that it is difficult to crush into uniform powder, and it is difficult to prepare polyimide foam with uniform pore size. Changing part of the dianhydride to tetraacid is one of the methods used to reduce the viscosity of the precursor solution when preparing polyimide materials, but there are basically no reports in the foam field. The invention prepares a series of polyimide foamed plastics with excellent performance by rationally regulating the types and ratios of tetraacids and dianhydrides, and completing foaming and imidization by one-step temperature rise.

发明内容Contents of the invention

本发明目的是为了克服现有技术的不足而提供一种新的合成方法来制备聚酰亚胺泡沫塑料,由芳香二胺、芳香二酐、芳香四酸及混合溶剂经由聚酰胺酸法形成低粘度前驱体溶液,干燥后可轻易破碎成粒径均匀的粉末,然后形成聚酰亚胺泡沫,是一种低成本、易加工的聚酰亚胺泡沫制备方法。The purpose of the present invention is to provide a new synthetic method to prepare polyimide foam plastics in order to overcome the deficiencies in the prior art, by aromatic diamine, aromatic dianhydride, aromatic four acid and mixed solvent to form low Viscosity precursor solution, after drying, can be easily crushed into powder with uniform particle size, and then form polyimide foam, which is a low-cost, easy-to-process polyimide foam preparation method.

为了达到上述目的,本发明采用的方案是:一种聚酰亚胺泡沫塑料制备方法,其包括以下步骤:In order to achieve the above object, the solution adopted in the present invention is: a polyimide foam preparation method, which comprises the following steps:

(1)在反应器中加入芳香二胺及低分子醇与四氢呋喃的混合溶剂,均匀搅拌后加入芳香二酐进行反应;(1) Add the mixed solvent of aromatic diamine and low-molecular alcohol and tetrahydrofuran in the reactor, add aromatic dianhydride after stirring evenly and react;

(2)在步骤(1)得到的反应溶液中加入芳香四酸,使芳香四酸的加入量以(芳香二酐+芳香四酸):芳香二胺的摩尔比为1:1,并继续进行反应得到聚酰亚胺前驱体溶液;(2) Add aromatic tetraacid to the reaction solution obtained in step (1), so that the amount of aromatic tetraacid added is (aromatic dianhydride+aromatic tetraacid): the molar ratio of aromatic diamine is 1:1, and continue Reaction obtains polyimide precursor solution;

(3)将步骤(2)的前驱体溶液干燥、粉碎成粉末后铺入模具中升温发泡得到最终的聚酰亚胺泡沫塑料。(3) Drying the precursor solution in step (2), pulverizing it into powder, spreading it into a mold, raising the temperature and foaming to obtain the final polyimide foam plastic.

上述的制备方法中,步骤(1)和步骤(2)为前驱体溶液的制备,在传统的方法之中,需要严格控制芳香二酐及芳香二胺的等摩尔比,以达到足够高本体粘度的聚酰亚胺前驱体溶液,否则会因为发泡时体系粘度太低导致并泡严重,甚至无法发泡的问题。然而高的前驱体溶液粘度难以进行诸如复合材料制备等进一步的加工,且二酐原料价格高昂,限制了聚酰亚胺泡沫的低成本要求领域的应用。而通过芳香四酸的加入,降低了前驱体溶液的粘度,易于生产加工,且维持了聚酰亚胺泡沫的性能。In the above preparation method, step (1) and step (2) are the preparation of precursor solution. In the traditional method, it is necessary to strictly control the equimolar ratio of aromatic dianhydride and aromatic diamine to achieve a sufficiently high bulk viscosity. Otherwise, the viscosity of the system is too low during foaming, which will cause serious foaming, or even the problem of not being able to foam. However, the high viscosity of the precursor solution is difficult for further processing such as the preparation of composite materials, and the price of the raw material of dianhydride is high, which limits the application of polyimide foam in the field of low cost requirements. The addition of the aromatic tetraacid reduces the viscosity of the precursor solution, facilitates production and processing, and maintains the performance of the polyimide foam.

在步骤(1)中,所述芳香二胺与芳香二酐的摩尔比例为100:90至100:50,优选100:90,100:80或100:70;所述低分子醇与四氢呋喃的比例为1:2~1:6,优选为1:4。In step (1), the molar ratio of the aromatic diamine to the aromatic dianhydride is 100:90 to 100:50, preferably 100:90, 100:80 or 100:70; the ratio of the low molecular weight alcohol to tetrahydrofuran 1:2 to 1:6, preferably 1:4.

所述混合溶剂量按照反应物占质量比10%~30%配置,优选为20%。The amount of the mixed solvent is configured according to the reactants accounting for 10%-30% by mass, preferably 20%.

所述芳香二胺可为二氨基二苯醚、二氨基二苯甲烷、对苯二胺、间苯二胺、二氨基吡啶和双酚A二醚二胺中的至少一种。The aromatic diamine may be at least one of diaminodiphenyl ether, diaminodiphenylmethane, p-phenylenediamine, m-phenylenediamine, diaminopyridine and bisphenol A diether diamine.

所述低分子醇可为碳原子数为1-4的脂肪醇,比如甲醇、乙醇、丙醇或正丁醇。The low-molecular-weight alcohol can be an aliphatic alcohol with 1-4 carbon atoms, such as methanol, ethanol, propanol or n-butanol.

所述芳香二酐可为3,3’,4,4’-二苯醚四酸二酐、3,3’,4,4’-二苯酮四酸二酐、3,3’,4,4’-三苯二醚四酸二酐、4,4’-六氟亚异丙基邻苯二甲酸酐、3,3’,4,4’-联苯四酸二酐、3,3’,4,4’-二苯砜四酸二酐和1,2,4,5-均苯四甲酸酐中的任一种。The aromatic dianhydride can be 3,3',4,4'-diphenyl ether tetraacid dianhydride, 3,3',4,4'-benzophenone tetraacid dianhydride, 3,3',4, 4'-triphenylene ether tetra-acid dianhydride, 4,4'-hexafluoroisopropylidene phthalic anhydride, 3,3',4,4'-biphenyl tetra-acid dianhydride, 3,3' , Any of 4,4'-diphenylsulfonetetracarboxylic dianhydride and 1,2,4,5-pyromellitic anhydride.

在步骤(2)中,芳香四酸可为均苯四甲酸、3,3’,4,4’-二苯酮四甲酸、3,3’,4,4’-联苯四甲酸中的至少一种。In step (2), the aromatic tetracarboxylic acid can be at least A sort of.

上述的制备方法步骤(2)中,所述反应之后,还包括在混合液中加入泡沫稳定剂的步骤;所述泡沫稳定剂可为聚二甲基硅氧烷、聚氧化乙烯型非离子表面活性剂或阳离子含氟表面活性剂;所述泡沫稳定剂的添加量可为所述芳香二酐、芳香二胺和芳香二酸的质量之和的0.5%~4%,具体可为2%。In the above-mentioned preparation method step (2), after the reaction, it also includes the step of adding a foam stabilizer in the mixed solution; the foam stabilizer can be polydimethylsiloxane, polyethylene oxide type nonionic surface Active agent or cationic fluorine-containing surfactant; the added amount of the foam stabilizer may be 0.5% to 4% of the mass sum of the aromatic dianhydride, aromatic diamine and aromatic diacid, specifically 2%.

上述的制备方法,步骤(1)中的反应温度可为20℃~50℃,优选为30℃。反应时间可为2h~12h,优选为4h~10h。In the above preparation method, the reaction temperature in step (1) may be 20°C to 50°C, preferably 30°C. The reaction time may be 2h-12h, preferably 4h-10h.

上述的制备方法,步骤(2)的反应温度保持与步骤(1)相同。反应时间可为1h~10h,优选为1h~4h。In the above-mentioned preparation method, the reaction temperature of step (2) remains the same as that of step (1). The reaction time may be 1h-10h, preferably 1h-4h.

上述的制备方法,步骤(3)中的干燥温度可为20℃~60℃,除去大部分溶剂。干燥条件为电热鼓风箱或是真空烘箱。In the above preparation method, the drying temperature in step (3) can be 20°C-60°C to remove most of the solvent. Drying conditions are electric blast box or vacuum oven.

上述的制备方法,步骤(3)中将干燥后的固体粉碎,可用粉碎机粉碎或是研磨粉碎。In the above preparation method, in step (3), the dried solid is pulverized, which can be pulverized by a pulverizer or ground.

上述的制备方法,步骤(3)中,发泡的温度可为200℃~300℃,优选为220℃~280℃。In the above preparation method, in step (3), the foaming temperature may be 200°C-300°C, preferably 220°C-280°C.

上述的制备方法,步骤(3)中,发泡的时间可为20min~2h,优选为1h。In the above preparation method, in step (3), the foaming time may be 20 minutes to 2 hours, preferably 1 hour.

优化地,所述方法步骤(3)在干燥时先在室温挥发掉大部分溶剂,之后使用真空烘箱真空干燥,所使用温度可为40℃~60℃,优选为60℃。干燥时间为4h~24h,优选为8h~12h。Optimally, in the step (3) of the method, most of the solvents are volatilized at room temperature before being dried in a vacuum oven at a temperature of 40°C to 60°C, preferably 60°C. The drying time is 4h-24h, preferably 8h-12h.

本发明进一步提供了一种由上述制备方法得到的聚酰亚胺泡沫塑料。The present invention further provides a polyimide foam obtained by the above preparation method.

与现有技术相比,本发明具有以下优点:本发明聚酰亚胺泡沫塑料的制备方法中,通过将部分芳香二酐与适当比例的芳香四酸置换,获得低本体粘度前驱体溶液同时又保持泡沫最终性能,同时保证了材料的发泡温度跟传统工艺相匹配。而芳香四酸的加入也降低了聚酰亚胺泡沫塑料的原料成本。同时本发明制备工艺简单,发泡与材料的聚酰亚胺化一步完成,不需再进一步的加工。本发明的聚酰亚胺泡沫塑料制备方法不需要另加发泡剂,而是直接使用低沸点溶剂直接发泡。所制备的泡沫呈现开闭孔结构,密度根据需要可为20-120Kg/m3,5%热失重可高达580℃(N2),氧指数介于38-42,随着芳香四酸加入量的增加,材料的压缩模量增加,而耐温性能保持一致。Compared with the prior art, the present invention has the following advantages: in the preparation method of the polyimide foam of the present invention, by substituting part of the aromatic dianhydride with an appropriate proportion of aromatic tetraacids, the precursor solution with low bulk viscosity is obtained and simultaneously Maintain the final performance of the foam, while ensuring that the foaming temperature of the material matches the traditional process. The addition of aromatic tetra-acid also reduces the raw material cost of polyimide foam. At the same time, the preparation process of the invention is simple, and the foaming and polyimidization of the material are completed in one step without further processing. The preparation method of the polyimide foamed plastics of the present invention does not need additional foaming agent, but directly uses low-boiling point solvent for direct foaming. The prepared foam presents an open and closed cell structure, the density can be 20-120Kg/m 3 according to needs, the 5% thermal weight loss can be as high as 580°C (N 2 ), and the oxygen index is between 38-42. With the increase of , the compressive modulus of the material increases, while the temperature resistance remains the same.

附图说明Description of drawings

图1是不同四酸加入量对于泡沫压缩强度的影响的曲线图。Figure 1 is a graph showing the effect of different tetraacid additions on foam compressive strength.

图2是四酸加入量对于泡沫玻璃化转变温度的影响的曲线图。Figure 2 is a graph of the effect of tetraacid addition on the glass transition temperature of foams.

具体实施方式detailed description

下面结合附图和实施例对本发明进一步详细说明。The present invention will be described in further detail below in conjunction with the accompanying drawings and embodiments.

下述实施例中所使用的实验方法如无特殊说明,均为常规方法The experimental methods used in the following examples are conventional methods unless otherwise specified.

下述实施例中所使用的材料、试剂等,如无特殊说明,均可从商业途径得到。The materials and reagents used in the following examples can be obtained from commercial sources unless otherwise specified.

实施例1Example 1

(1)将20.02g(0.1mol)的4’4–二氨基二苯醚与40.38g的甲醇、161.53g的四氢呋喃混合均匀后加入27.92g(0.09mol)的3,3’,4,4’-二苯醚四酸二酐,在50℃下反应4小时,之后加入2.54g(0.01mol)的均苯四甲酸继续反应4小时得到聚酰亚胺前驱体溶液。(1) Mix 20.02g (0.1mol) of 4'4-diaminodiphenyl ether with 40.38g of methanol and 161.53g of tetrahydrofuran and add 27.92g (0.09mol) of 3,3',4,4' - diphenyl ether tetra-acid dianhydride, react at 50° C. for 4 hours, then add 2.54 g (0.01 mol) of pyromellitic acid and continue the reaction for 4 hours to obtain a polyimide precursor solution.

(2)将步骤(1)的溶液室温干燥,之后放入60℃的真空烘箱中真空干燥10小时形成易碎固体。取出后粉碎成均匀粒径粉末。(2) The solution in step (1) was dried at room temperature, and then placed in a vacuum oven at 60° C. for 10 hours to form a brittle solid. Take it out and crush it into powder with uniform particle size.

(3)将步骤(2)中的粉末铺平于体积为1670cm3的模具之中,放入250℃的高温炉中闭模发泡1小时,得到最终的聚酰亚胺泡沫塑料。(3) Spread the powder in step (2) in a mold with a volume of 1670 cm 3 , put it into a high-temperature furnace at 250° C. for closed mold foaming for 1 hour to obtain the final polyimide foam.

对本实施例中的聚酰亚胺泡沫塑料进行性能测定,该泡沫的密度为33.3Kg/m3,玻璃化转变温度为275℃,5%热失重为570℃,室温下压缩至10%的压缩强度为0.034MPa,压缩模量为0.31MPa,极限氧指数,50%。The performance of the polyimide foam in this example is measured. The density of the foam is 33.3Kg/m 3 , the glass transition temperature is 275°C, the 5% thermal weight loss is 570°C, and it is compressed to 10% compression at room temperature. The strength is 0.034MPa, the compressive modulus is 0.31MPa, and the limiting oxygen index is 50%.

实施例2Example 2

(1)将20.02g(0.1mol)的4’4–二氨基二苯醚与40.38g的甲醇、161.53g的四氢呋喃混合均匀后加入21.71g(0.07mol)的3,3’,4,4’-二苯醚四酸二酐,在30℃下反应2小时,之后加入7.62g(0.03mol)的均苯四甲酸继续反应1小时后加入1.03g聚二甲基硅氧烷得到聚酰亚胺前驱体溶液。(1) Mix 20.02g (0.1mol) of 4'4-diaminodiphenyl ether with 40.38g of methanol and 161.53g of tetrahydrofuran, then add 21.71g (0.07mol) of 3,3',4,4' -Diphenyl ether tetraacid dianhydride, react at 30°C for 2 hours, then add 7.62g (0.03mol) of pyromellitic acid to continue the reaction for 1 hour, then add 1.03g of polydimethylsiloxane to obtain polyimide precursor solution.

(2)将步骤(1)的溶液倒出至其不再流动后,放入60℃的真空烘箱中真空干燥20小时形成易碎固体。取出后粉碎成均匀粒径粉末。(2) Pour out the solution in step (1) until it stops flowing, and then put it into a vacuum oven at 60° C. for 20 hours to vacuum dry to form a brittle solid. Take it out and crush it into powder with uniform particle size.

(3)将步骤(2)中的粉末铺平于体积为960cm3的模具之中,放入240℃的高温炉中闭模发泡1小时,得到最终的聚酰亚胺泡沫塑料。(3) Spread the powder in step (2) in a mold with a volume of 960 cm 3 , put it into a high-temperature furnace at 240° C. for closed mold foaming for 1 hour to obtain the final polyimide foam.

对本实施例中的聚酰亚胺泡沫塑料进行性能测定,该泡沫的密度为47.5Kg/m3,玻璃化转变温度为277℃,5%热失重为564℃,室温下的压缩强度为0.056MPa,压缩模量为0.56MPa,极限氧指数为49.8%。The properties of the polyimide foam in this example were measured. The foam had a density of 47.5Kg/m 3 , a glass transition temperature of 277°C, a 5% thermal weight loss of 564°C, and a compressive strength of 0.056MPa at room temperature. , the compressive modulus is 0.56MPa, and the limiting oxygen index is 49.8%.

实施例3Example 3

(1)将19.83g(0.1mol)的4’4–二氨基二苯甲烷与40.23g的甲醇、160.93g的四氢呋喃混合均匀后加入27.92g(0.09mol)的3,3’,4,4’-二苯醚四酸二酐,在40℃下反应6小时,之后加入2.54g(0.01mol)的均苯四甲酸继续反应4小时后加入1.03g聚二甲基硅氧烷得到聚酰亚胺前驱体溶液。(1) Mix 19.83g (0.1mol) of 4'4-diaminodiphenylmethane with 40.23g of methanol and 160.93g of tetrahydrofuran and add 27.92g (0.09mol) of 3,3',4,4' -Diphenyl ether tetraacid dianhydride, react at 40°C for 6 hours, then add 2.54g (0.01mol) of pyromellitic acid to continue the reaction for 4 hours, then add 1.03g of polydimethylsiloxane to obtain polyimide precursor solution.

(2)将步骤(1)的溶液倒入容器中,待其不再流动后放入40℃的真空烘箱中真空干燥10小时形成易碎固体。取出后粉碎成均匀粒径粉末。(2) Pour the solution of step (1) into a container, put it into a vacuum oven at 40° C. for 10 hours and vacuum dry it to form a brittle solid after it stops flowing. Take it out and crush it into powder with uniform particle size.

(3)将步骤(2)中的粉末铺平于体积为1670cm3的模具之中,放入250℃的高温炉中闭模发泡1小时,得到最终的聚酰亚胺泡沫塑料。(3) Spread the powder in step (2) in a mold with a volume of 1670 cm 3 , put it into a high-temperature furnace at 250° C. for closed mold foaming for 1 hour to obtain the final polyimide foam.

对本实施例中的聚酰亚胺泡沫塑料进行性能测定,该泡沫的密度为37.8Kg/m3,玻璃化转变温度为273℃,5%热失重为569℃,室温下压缩至10%的压缩强度为0.044KPa,压缩模量为0.38MPa,极限氧指数,50%。The performance of the polyimide foam in this example is measured. The density of the foam is 37.8Kg/m 3 , the glass transition temperature is 273°C, the 5% thermal weight loss is 569°C, and it is compressed to 10% compression at room temperature. The strength is 0.044KPa, the compression modulus is 0.38MPa, and the limiting oxygen index is 50%.

实施例4Example 4

(1)将20.02g(0.1mol)的4’4–二氨基二苯醚与40.38g的甲醇、161.53g的四氢呋喃混合均匀后加入215.51g(0.05mol)的3,3’,4,4’-二苯醚四酸二酐,在20℃下反应4小时,之后加入12.7g(0.05mol)的均苯四甲酸继续反应1小时后加入1.03g聚二甲基硅氧烷得到聚酰亚胺前驱体溶液。(1) Mix 20.02g (0.1mol) of 4'4-diaminodiphenyl ether with 40.38g of methanol and 161.53g of tetrahydrofuran and add 215.51g (0.05mol) of 3,3',4,4' -Diphenyl ether tetraacid dianhydride, react at 20°C for 4 hours, then add 12.7g (0.05mol) of pyromellitic acid to continue the reaction for 1 hour, then add 1.03g of polydimethylsiloxane to obtain polyimide precursor solution.

(2)将步骤(1)的溶液室温干燥,之后放入30℃的真空烘箱中真空干燥10小时形成易碎固体。取出后粉碎成均匀粒径粉末。(2) The solution in step (1) was dried at room temperature, and then placed in a vacuum oven at 30° C. for 10 hours to form a brittle solid. Take it out and crush it into powder with uniform particle size.

(3)将步骤(2)中的粉末铺平于体积为1670cm3的模具之中,放入260℃的高温炉中闭模发泡1小时,得到最终的聚酰亚胺泡沫塑料。(3) Spread the powder in step (2) in a mold with a volume of 1670 cm 3 , put it into a high-temperature furnace at 260° C. for closed mold foaming for 1 hour to obtain the final polyimide foam.

对本实施例中的聚酰亚胺泡沫塑料进行性能测定,该泡沫的密度为33.0Kg/m3,玻璃化转变温度为261℃,5%热失重为565℃,室温下压缩至10%的压缩强度为0.029KPa,压缩模量为0.28MPa,极限氧指数,48%。The performance of the polyimide foam in this example is measured. The density of the foam is 33.0Kg/m 3 , the glass transition temperature is 261°C, the 5% thermal weight loss is 565°C, and it is compressed to 10% compression at room temperature. The strength is 0.029KPa, the compression modulus is 0.28MPa, and the limiting oxygen index is 48%.

实施例5Example 5

(1)将20.02g(0.1mol)的4’4–二氨基二苯甲烷与24.06g的甲醇、96.24g的四氢呋喃混合均匀后加入29.00g(0.09mol)的3,3’4,4’-二苯甲酮四羧酸二酐,在30℃下反应4小时,之后加入2.54g(0.01mol)的均苯四甲酸继续反应2小时后加入1.03g聚二甲基硅氧烷得到聚酰亚胺前驱体溶液。(1) Mix 20.02g (0.1mol) of 4'4-diaminodiphenylmethane with 24.06g of methanol and 96.24g of tetrahydrofuran and add 29.00g (0.09mol) of 3,3'4,4'- Benzophenone tetracarboxylic dianhydride was reacted at 30°C for 4 hours, then 2.54g (0.01mol) of pyromellitic acid was added to continue the reaction for 2 hours, and then 1.03g of polydimethylsiloxane was added to obtain polyimellitic acid. Amine precursor solution.

(2)将步骤(1)的溶液室温干燥,之后放入70℃的真空烘箱中真空干燥10小时形成易碎固体。取出后粉碎成均匀粒径粉末。(2) The solution in step (1) was dried at room temperature, and then placed in a vacuum oven at 70° C. for 10 hours to form a brittle solid. Take it out and crush it into powder with uniform particle size.

(3)将步骤(2)中的粉末铺平于体积为1670cm3的模具之中,放入280℃的高温炉中闭模发泡1小时,得到最终的聚酰亚胺泡沫塑料。(3) Spread the powder in step (2) in a mold with a volume of 1670 cm 3 , put it into a high-temperature furnace at 280° C. for closed mold foaming for 1 hour to obtain the final polyimide foam.

对本实施例中的聚酰亚胺泡沫塑料进行性能测定,该泡沫的密度为34.5Kg/m3,玻璃化转变温度为263℃,5%热失重为563℃,室温下压缩至10%的压缩强度为0.047KPa,压缩模量为0.40MPa,极限氧指数,47%。The performance of the polyimide foam in this example is measured. The density of the foam is 34.5Kg/m 3 , the glass transition temperature is 263°C, the 5% thermal weight loss is 563°C, and it is compressed to 10% compression at room temperature. The strength is 0.047KPa, the compressive modulus is 0.40MPa, and the limiting oxygen index is 47%.

上述的各个实施例只是为了说明本发明的技术方法及核心思想,让涉及本领域的人员能够具体了解本发明的内容并具体实施,并不能以此限制本发明的保护范围。此外在不脱离本发明原理下所做的修饰和改进也应当涵盖在本发明的保护范围之内。The above-mentioned embodiments are only to illustrate the technical method and core idea of the present invention, so that those skilled in the art can specifically understand the content of the present invention and implement it, and cannot limit the protection scope of the present invention. In addition, modifications and improvements made without departing from the principles of the present invention should also be covered within the protection scope of the present invention.

Claims (10)

1. a kind of preparation method of polyimide foam, it is characterised in that comprise the following steps:
(1) mixed solvent of aromatic diamines and low mass molecule alcohol and tetrahydrofuran is added in the reactor, is uniformly stirred Aromatic dianhydride is added to be reacted after mixing;
(2) fragrant tetracid is added in the reaction solution that step (1) is obtained, make the addition of fragrant tetracid with (aromatic dianhydride+fragrance tetracid):The mol ratio of aromatic diamines is 1:1, and proceeding reaction, to obtain polyamides sub- Amine precursor solution;
(3) precursor solution that obtains step (2) dries, be ground into after powder to spread and heat up in mould hair Bubble obtains final polyimide foam.
2. preparation method according to claim 1, it is characterised in that:Low point described in step (1) The ratio of sub- alcohol and tetrahydrofuran is 1:2~1:6;The mixed solvent amount accounts for mass ratio according to reactant 10%~30% configuration;The aromatic diamines be diaminodiphenyl ether, MDA, p-phenylenediamine, At least one in phenylenediamine, diamino-pyridine and the ether diamine of bisphenol-A two;The low mass molecule alcohol is carbon number It is the fatty alcohol of 1-4;The aromatic dianhydride be 3,3 ', 4,4 '-oxydiphthalic, 3,3 ', 4, 4 '-benzophenone tetracarboxylic dianhydride, 3,3 ', 4,4 '-triphen diether tetracarboxylic dianhydride, 4,4 '-hexafluoro Asia isopropyl Base phthalic anhydride, 3,3 ', 4,4 '-BPDA, 3,3 ', 4,4 '-diphenyl sulphone (DPS) tetracid Any one in dianhydride and 1,2,4,5- pyromellitic dianhydrides;The aromatic dianhydride and aromatic diamines mole Than being 100:90 to 100:50;The reaction temperature is 20 DEG C~50 DEG C;The reaction time is 2h~12h.
3. preparation method according to claim 1 and 2, it is characterised in that:Described in step (1) The ratio of low mass molecule alcohol and tetrahydrofuran is specially 1:4;The mixed solvent amount is specially and accounts for matter according to reactant Amount is configured than 20%;The low mass molecule alcohol is methyl alcohol, ethanol, propyl alcohol or n-butanol;The aromatic dianhydride and virtue The mol ratio of fragrant diamines is 100:90,100:80 or 100:70;The reaction temperature is 30 DEG C;The reaction Time is 4h~10h.
4. preparation method according to claim 1 and 2, it is characterised in that:Described in step (2) Fragrant tetracid is Pyromellitic Acid, 3,3 ', 4,4 '-benzophenone tetracarboxylic, 3,3 ', 4,4 '-biphenyl At least one in tetracarboxylic acid;It is additionally included in step (2) in precursor solution and adds foam stabiliser;Institute Foam stabiliser is stated for dimethyl silicone polymer, polyoxyethylene ene-type nonionic surfactant or cationic fluorochemical Surfactant;The addition of the foam stabiliser is the quality sum of the aromatic dianhydride and aromatic diamines 0.5%~4%;Reaction temperature is identical with step (1), and the reaction time is 1h~10h.
5. preparation method according to claim 3, it is characterised in that:Fragrance described in step (2) Tetracid is Pyromellitic Acid, 3,3 ', 4,4 '-benzophenone tetracarboxylic, 3,3 ', 4,4 '-biphenyl tetracarboxylic At least one in acid;It is additionally included in step (2) in precursor solution and adds foam stabiliser;The bubble Foam stabilizers are dimethyl silicone polymer, polyoxyethylene ene-type nonionic surfactant or cationic fluorosurfactants Activating agent;The addition of the foam stabiliser is the quality sum of the aromatic dianhydride and aromatic diamines 0.5%~4%;Reaction temperature is identical with step (1), and the reaction time is 1h~10h.
6. preparation method according to claim 1 and 2, it is characterised in that:Step also includes in (2) Foam stabiliser is added in precursor solution;The foam stabiliser is dimethyl silicone polymer, polyoxyethylene Ene-type nonionic surfactant or cationic fluorosurfactants activating agent;The addition of the foam stabiliser is institute State the 2% of the quality sum of aromatic dianhydride and aromatic diamines;Reaction temperature is identical with step (1), the reaction time It is 1h-4h.
7. preparation method according to claim 4, it is characterised in that:The addition of the foam stabiliser Measure 2% of the quality sum for the aromatic dianhydride and aromatic diamines;Reaction temperature is identical with step (1), instead It is 1h-4h between seasonable.
8. preparation method according to claim 1 and 2, it is characterised in that:Drying in step (3) Temperature is 20 DEG C~60 DEG C, and drying time is 4h~24h;The temperature of foaming be 200 DEG C~300 DEG C, foaming when Between be 20min~2h;.
9. preparation method according to claim 4, it is characterised in that:Drying temperature is in step (3) 40 DEG C~60 DEG C, drying time is 8h~12h;The temperature of foaming is 220 DEG C~280 DEG C, and the time of foaming is 1h;.
10. the polyimide foam that the preparation method any one of claim 1-9 is obtained.
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EP1000109A2 (en) * 1998-05-29 2000-05-17 The Government of the United States of America as represented by the Administrator of the National Aeronautics and Space Adm. Polyimide precursor solid residuum
EP1002006B1 (en) * 1998-05-29 2005-03-23 The Government of the U.S.A., as represented by the Administrator of the National Aeronautics and Space Administration (NASA) Aromatic polyimide foam
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