JPH11171990A - Wholly aromatic polyimide precursor powder and its production - Google Patents

Wholly aromatic polyimide precursor powder and its production

Info

Publication number
JPH11171990A
JPH11171990A JP34262697A JP34262697A JPH11171990A JP H11171990 A JPH11171990 A JP H11171990A JP 34262697 A JP34262697 A JP 34262697A JP 34262697 A JP34262697 A JP 34262697A JP H11171990 A JPH11171990 A JP H11171990A
Authority
JP
Japan
Prior art keywords
polyimide precursor
polyimide
powder
solvent
aromatic
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP34262697A
Other languages
Japanese (ja)
Inventor
Mikio Furukawa
幹夫 古川
Yoshihisa Yamada
良尚 山田
Nagayasu Kaneshiro
永泰 金城
Yoshiaki Echigo
良彰 越後
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Unitika Ltd
Original Assignee
Unitika Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Unitika Ltd filed Critical Unitika Ltd
Priority to JP34262697A priority Critical patent/JPH11171990A/en
Publication of JPH11171990A publication Critical patent/JPH11171990A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain the subject powder excellent in stability, capable of being converted into a polyimide with a high polymerization degree and useful for molding a polyimide by mixing an aromatic diamine and a diester of a specific aromatic tetracarboxylic acid. SOLUTION: This powder comprises a salt composed of (A) an aromatic diamine and (B) a salt formed out of a diester of an aromatic tetracarbocylic acid of the formula (R is a 1-5C alkyl). For example, the component A is mixed with the component B in nearly same mols in the solvent, and a poor solvent for the polyimide precursor such as water or a water-soluble alcohol of up to twice of the amount of the liquid is added to the suspension of the obtained polyimide precursor or a solution of the polyimide precursor to precipitate the polyimide precursor powder. The obtained precipitate is filtered, and dried to remove the solvent and to provide the objective powder with the particle diameter of about 5-150 μm. The powder is heated and baked to carrying out the imide cyclization and to provide a polyimide.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、全芳香族ポリイミ
ド前駆体粉体及びその製造方法に関する。
TECHNICAL FIELD The present invention relates to a wholly aromatic polyimide precursor powder and a method for producing the same.

【0002】[0002]

【従来の技術】ポリイミド樹脂はその化学構造によっ
て、種々特性が変化することが知られており、特に、全
芳香族ポリイミドはその優れた耐熱性、機械特性、摺動
特性から近年、電子、電気産業、自動車産業、宇宙、航
空産業などにおいて注目を集めているエンジニアプラス
チックの一つであり、高い需要が見込まれている。一般
に、全芳香族ポリイミドは熱軟化点を有さず、また、溶
剤に不溶のため成形が困難であることが多く、このた
め、これら問題点を改善する目的で種々の検討がおこな
われてきた。多くの場合、アミド結合を有するポリイミ
ド前駆体であるポリアミド酸(ポリマー)を成形し、こ
れをポリイミドに変換する方法が行われている。
2. Description of the Related Art Polyimide resins are known to have various characteristics depending on their chemical structures. In particular, wholly aromatic polyimides have recently been used in electronic and electrical applications due to their excellent heat resistance, mechanical properties and sliding properties. It is one of the engineering plastics that has attracted attention in industries such as industry, automobile industry, space and aviation industry, and high demand is expected. In general, wholly aromatic polyimides do not have a thermal softening point, and are often difficult to mold due to insolubility in a solvent. For this reason, various studies have been made to improve these problems. . In many cases, a method is used in which a polyamic acid (polymer), which is a polyimide precursor having an amide bond, is molded and converted into a polyimide.

【0003】ポリイミド前駆体粉体を得る方法として
は、一つにはポリイミド前駆体溶液(ポリアミド酸溶
液)を貧溶媒に混合し、溶解しているポリイミド前駆体
を析出させる方法が特開平1−292035号公報、特
開平4−272934号公報もしくは特開平4−272
936号公報などに開示されている。しかしながら、こ
の方法によると、ポリイミド前駆体(ポリアミド酸)の
溶媒に対する溶解度差を利用しているため、使用する貧
溶媒がポリアミド酸に対して大量に必要であり、かつ、
ポリアミド酸溶液と貧溶媒の混合条件を厳密に制御しな
ければならないといった問題を有していた。また、ポリ
アミド酸は加水分解により重合度が低下しやすい傾向に
ありその取扱いに注意が必要であった。
One method for obtaining a polyimide precursor powder is to mix a polyimide precursor solution (polyamic acid solution) with a poor solvent to precipitate a dissolved polyimide precursor. JP-A-292035, JP-A-4-272934 or JP-A-4-272
No. 936, and the like. However, according to this method, since a difference in solubility of the polyimide precursor (polyamic acid) in the solvent is used, a large amount of poor solvent to be used is required for the polyamic acid, and
There was a problem that the mixing conditions of the polyamic acid solution and the poor solvent had to be strictly controlled. In addition, the degree of polymerization of polyamic acid tends to decrease due to hydrolysis, and care must be taken when handling the polyamic acid.

【0004】また、第二の方法としては、特開平5−2
71539号公報、特開平5−202763号公報もし
くは特開平5−2202764号公報に開示されている
ように、水溶性ケトンもしくは水溶性エーテルを溶媒と
する系中に懸濁しているポリイミド前駆体を分離する方
法がある。この方法によれば、容易にポリイミド前駆体
粉体を得ることができるが、得られるポリイミド前駆体
は上記方法と同じく高重合度のポリアミド酸であり、加
水分解により重合度が低下しやすい傾向にある点は改善
するに至っていなかった。
A second method is disclosed in Japanese Patent Laid-Open No.
As disclosed in JP-A-71539, JP-A-5-202763 or JP-A-5-2202764, a polyimide precursor suspended in a system using a water-soluble ketone or a water-soluble ether as a solvent is separated. There is a way to do that. According to this method, a polyimide precursor powder can be easily obtained, but the obtained polyimide precursor is a polyamic acid having a high degree of polymerization as in the above method, and the degree of polymerization tends to decrease due to hydrolysis. Some things had not improved.

【0005】なお、特公平2−48571号公報には、
生成するポリイミドの貧溶媒中で、芳香族テトラカルボ
ン酸二無水物と芳香族ジアミンよりなるモノマー成分を
ポリイミドの貧溶媒に溶解して均一な溶液とし、加熱し
てポリイミド粒子を析出させ、分離してポリイミド粉末
を得る方法が開示されている。しかし、この方法におい
ても、モノマーを溶解している均一な溶液においてはモ
ノマー同士が反応して前記と同様にポリアミド酸となっ
てポリマーが溶媒に溶解しているものであった。
[0005] Japanese Patent Publication No. 2-48571 discloses that
In the poor solvent of the resulting polyimide, the monomer component consisting of aromatic tetracarboxylic dianhydride and aromatic diamine is dissolved in the poor solvent of the polyimide to form a uniform solution, and the polyimide particles are precipitated by heating and separated. A method for obtaining a polyimide powder by using the method is disclosed. However, even in this method, in a uniform solution in which the monomers are dissolved, the monomers react with each other to form polyamic acid as described above, and the polymer is dissolved in the solvent.

【0006】[0006]

【発明が解決しようとする課題】このような状況に鑑
み、本発明の課題は、安定性に優れており、高重合度の
ポリイミドに変換することができて、ポリイミドの成形
に好適に利用できるポリイミド前駆体粉体の提供、及び
このようなポリイミド前駆体粉体を安価に、しかも容易
に製造することができる全芳香族ポリイミド前駆体粉体
の製造方法を提供することにある。
SUMMARY OF THE INVENTION In view of such circumstances, an object of the present invention is to provide a polyimide which has excellent stability, can be converted into a polyimide having a high degree of polymerization, and can be suitably used for molding polyimide. An object of the present invention is to provide a polyimide precursor powder and a method for producing a wholly aromatic polyimide precursor powder capable of easily and inexpensively producing such a polyimide precursor powder.

【0007】[0007]

【課題を解決するための手段】本発明者らは、上記課題
を解決するために鋭意検討した結果、溶媒中で芳香族ジ
アミンと特定の芳香族テトラカルボン酸ジエステルを混
合後、得られる溶液もしくは懸濁液からポリイミド前駆
体を単離することにより得られる粉体を加熱焼成すると
イミド閉環し、ポリイミドが生成するという知見を得、
かかる知見に基づき、本発明に到達した。
Means for Solving the Problems The present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, obtained by mixing an aromatic diamine and a specific aromatic tetracarboxylic acid diester in a solvent, and When the powder obtained by isolating the polyimide precursor from the suspension was heated and calcined, the imide was closed, and the finding that polyimide was formed was obtained.
Based on such findings, the present invention has been achieved.

【0008】すなわち、本発明の要旨は、第1に、芳香
族ジアミンと構造式(1)に示す芳香族テトラカルボン
酸ジエステルとから形成されている塩からなる全芳香族
ポリイミド前駆体粉体であり、第2に、芳香族ジアミン
と構造式(1)に示す芳香族テトラカルボン酸ジエステ
ルとを溶媒中で混合して塩を形成させて、溶媒を除去し
て単離することを特徴とする全芳香族ポリイミド前駆体
粉体の製造方法である。なお、Rは炭素数1〜5のアル
キル基を示す。
That is, the gist of the present invention is, first, a wholly aromatic polyimide precursor powder comprising a salt formed from an aromatic diamine and an aromatic tetracarboxylic diester represented by the structural formula (1). Second, an aromatic diamine and an aromatic tetracarboxylic acid diester represented by the structural formula (1) are mixed in a solvent to form a salt, and the solvent is removed to isolate. This is a method for producing a wholly aromatic polyimide precursor powder. R represents an alkyl group having 1 to 5 carbon atoms.

【0009】[0009]

【化3】 Embedded image

【0010】[0010]

【発明の実施の形態】以下に、本発明について詳細に説
明する。本発明のポリイミド前駆体粉体は、芳香族ジア
ミンと構造式(1)に示す芳香族テトラカルボン酸ジエ
ステルとから形成されている塩よりなり、ポリイミド前
駆体はイミド閉環して下記繰り返し単位よりなるポリイ
ミドを生成する。ここで、イミド閉環とは熱的もしくは
化学的反応によるイミド環の生成をいう。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail. The polyimide precursor powder of the present invention comprises a salt formed from an aromatic diamine and an aromatic tetracarboxylic acid diester represented by the structural formula (1). Produce polyimide. Here, imide ring closure refers to the formation of an imide ring by a thermal or chemical reaction.

【0011】[0011]

【化4】 Embedded image

【0012】なお、Rは炭素数1〜5のアルキル基を示
し、炭素数1又は2のメチル基又はエチル基であるもの
が製造上好ましい。また、R’は少なくとも1つの炭素
6員環を持つ2価の芳香族残基を示す。なお、代表的な
ポリイミド前駆体であるポリアミド酸が、下記一般式
(2)に示すような酸とアミンとの間にアミド結合を有
する繰り返し単位からなるポリマーであるのに対して、
塩はこのようなアミド結合を有さず、酸とアミンの間に
弱い相互作用(イオン結合)を有する形態であると考え
られる。
R represents an alkyl group having 1 to 5 carbon atoms, preferably a methyl or ethyl group having 1 or 2 carbon atoms in terms of production. R ′ represents a divalent aromatic residue having at least one carbon 6-membered ring. In addition, polyamic acid, which is a typical polyimide precursor, is a polymer including a repeating unit having an amide bond between an acid and an amine as shown in the following general formula (2),
It is considered that the salt does not have such an amide bond and is in a form having a weak interaction (ionic bond) between the acid and the amine.

【0013】[0013]

【化5】 Embedded image

【0014】したがって、種々の溶媒中に本発明によっ
て得られるポリイミド前駆体粉体を溶解しても、ただ単
にモノマーが分散した溶液であることから、ポリマー溶
液のように濃度や重合度が上がるにつれて急激に溶液の
粘度が上昇するような特性を示さない。
Therefore, even if the polyimide precursor powder obtained according to the present invention is dissolved in various solvents, it is merely a solution in which the monomer is dispersed. It does not exhibit such a property that the viscosity of the solution rapidly increases.

【0015】本発明におけるポリイミド前駆体における
R’の元となる芳香族ジアミンとしては下記構造式群に
示されるものが挙げられ、これらの中から選ばれる1種
もしくは複数種の混合物を用いることができる。
The aromatic diamine which is the source of R 'in the polyimide precursor according to the present invention includes those represented by the following structural formulas, and one or more kinds of mixtures selected from these may be used. it can.

【0016】[0016]

【化6】 Embedded image

【0017】本発明のポリイミド前駆体粉体は、芳香族
ジアミンと芳香族テトラカルボン酸ジエステルが略等モ
ル、すなわち、芳香族ジアミン1モルに対して、芳香族
テトラカルボン酸ジエステル0.9〜1.1モルから形
成されていることが好ましい。ポリイミド前駆体粉体
が、略等モルでない組成から形成されている場合、イミ
ド閉環してポリイミドに変換したときに、等モルより過
剰のモノマー成分がポリイミド中に残存したり、ポリイ
ミドの重合度が大きく低下し、ポリイミド本来の特性を
有することができなくなる傾向にあるため好ましくな
い。
In the polyimide precursor powder of the present invention, the aromatic diamine and the aromatic tetracarboxylic acid diester are almost equimolar, that is, the aromatic tetracarboxylic acid diester is 0.9 to 1 mole per mole of the aromatic diamine. .1 mol. When the polyimide precursor powder is formed from a composition that is not approximately equimolar, when the imide is closed and converted into polyimide, an excess of monomer components in equimolar remains in the polyimide or the degree of polymerization of the polyimide is reduced. This is not preferable because it tends to greatly decrease and lose the inherent properties of polyimide.

【0018】本発明のポリイミド前駆体粉体は、溶媒中
で略等モルの芳香族ジアミンと芳香族テトラカルボン酸
ジエステルを混合して製造される。略等モルの芳香族ジ
アミンと芳香族テトラカルボン酸ジエステルを混合する
と、ポリイミド前駆体粒子が分散した懸濁液もしくはポ
リイミド前駆体の溶液が得られる。この際、反応系中に
芳香族ジアミンと芳香族テトラカルボン酸ジエステルを
そのまま加えても良いし、一方もしくは両方を溶媒に溶
解してその溶液を反応系中に添加しても良い。芳香族ジ
アミンと芳香族テトラカルボン酸ジエステルの添加順序
は特に限定されないが、芳香族テトラカルボン酸ジエス
テルを溶媒に溶解もしくは分散した系に芳香族ジアミン
を添加する方が短時間で均一に混合できる傾向にある。
The polyimide precursor powder of the present invention is produced by mixing approximately equimolar amounts of an aromatic diamine and an aromatic tetracarboxylic acid diester in a solvent. When approximately equimolar amounts of the aromatic diamine and the aromatic tetracarboxylic acid diester are mixed, a suspension in which the polyimide precursor particles are dispersed or a solution of the polyimide precursor is obtained. At this time, the aromatic diamine and the aromatic tetracarboxylic acid diester may be added to the reaction system as they are, or one or both of them may be dissolved in a solvent and the solution may be added to the reaction system. The order of addition of the aromatic diamine and the aromatic tetracarboxylic diester is not particularly limited, but the addition of the aromatic diamine to a system in which the aromatic tetracarboxylic diester is dissolved or dispersed in a solvent tends to allow uniform mixing in a short time. It is in.

【0019】溶媒中で略等モルの芳香族ジアミンと芳香
族テトラカルボン酸ジエステルを混合したとき、ポリイ
ミド前駆体の懸濁液もしくは溶液のいずれが得られるか
は、ポリイミド前駆体の溶媒に対する溶解度によって左
右される。そして、溶媒中のポリイミド前駆体粒子の分
散濃度又はポリイミド前駆体の溶液濃度は、例えば、
N,N−ジメチルホルムアミドの場合、15〜60重量
%となるようにすることが好ましい。15重量%未満で
はポリイミド前駆体の溶解度よりもはるかに小さいため
溶液となり、このような希薄な溶液からはポリイミド前
駆体粉体を単離するのが困難になり生産性に欠ける。一
方、60重量%を超えたものは懸濁液となってはいるが
懸濁液の流動性が悪くなり、均一に混合できないなど取
り扱いに劣るばかりでなく、芳香族テトラカルボン酸ジ
エステルと芳香族ジアミンが十分に混合されず、均質な
ポリイミド前駆体を得るのが困難になる傾向にある。
When approximately equimolar amounts of an aromatic diamine and an aromatic tetracarboxylic acid diester are mixed in a solvent, whether a polyimide precursor suspension or a solution is obtained depends on the solubility of the polyimide precursor in the solvent. It depends. And the dispersion concentration of the polyimide precursor particles in the solvent or the solution concentration of the polyimide precursor is, for example,
In the case of N, N-dimethylformamide, the content is preferably 15 to 60% by weight. If the amount is less than 15% by weight, the solubility of the polyimide precursor is much smaller than the solubility of the polyimide precursor, so that it becomes difficult to isolate the polyimide precursor powder from such a dilute solution, and the productivity is lacking. On the other hand, if the amount exceeds 60% by weight, the suspension becomes a suspension, but the fluidity of the suspension deteriorates, and the suspension cannot be uniformly mixed. Diamines are not sufficiently mixed, and it tends to be difficult to obtain a homogeneous polyimide precursor.

【0020】上記のようにして得たポリイミド前駆体の
懸濁液もしくはポリイミド前駆体溶液に、液の2倍量ま
での水や水溶性アルコールなどのポリイミド前駆体の貧
溶媒を加えるとポリイミド前駆体粒子が析出してくるの
で濾過及び乾燥により、容易に溶媒を除去でき、5〜1
50μm程度の粒径の目的とするポリイミド前駆体粉体
を単離することができる。また、例えば15〜40重量
%のポリイミド前駆体を溶解したN,N−ジメチルホル
ムアミド溶液では溶媒に溶解しているポリイミド前駆体
成分を上記のようにして析出させずに、そのまま乾燥機
などによって、溶媒のみを蒸散させて濃度を上げていく
と、溶液からポリイミド前駆体粒子が析出してくるの
で、目的とするポリイミド前駆体粉体を単離することが
できる。
When a poor solvent for the polyimide precursor such as water or a water-soluble alcohol is added up to twice the amount of the polyimide precursor suspension or the polyimide precursor solution obtained above, the polyimide precursor Since the particles are precipitated, the solvent can be easily removed by filtration and drying.
A target polyimide precursor powder having a particle size of about 50 μm can be isolated. Further, for example, in a N, N-dimethylformamide solution in which 15 to 40% by weight of a polyimide precursor is dissolved, the polyimide precursor component dissolved in the solvent is not precipitated as described above, and is directly dried by a dryer or the like. As the concentration of the solvent is increased by evaporating only the solvent, polyimide precursor particles are precipitated from the solution, so that the target polyimide precursor powder can be isolated.

【0021】本発明のポリイミド前駆体粉体の製造に用
いられる溶媒は生成するポリイミド前駆体を粉体として
単離できる溶媒が好ましく、例えばN,N−ジメチルホ
ルムアミドに代表されるアミド系溶媒やジオキサンなど
の水溶性エーテル、アセトンに代表される水溶性ケトン
もしくはメタノールに代表される水溶性アルコールの類
から選択できる。これらの溶媒種中、N,N−ジメチル
ホルムアミド、N,N−ジメチルアセトアミド、N−メ
チルピロリドン、ジオキサン、テトラヒドロフラン、ア
セトンもしくはメタノールが好ましく、また、これらの
組み合わせからなる複数種の混合溶媒でもかまわない。
さらに、本発明の実施を妨げない範囲で、その他種々の
溶媒を上記溶媒に混合して合成溶媒として用いても差し
支えない。反応系中の温度は特に制御する必要はなく、
常温で行ってもよい。
The solvent used for producing the polyimide precursor powder of the present invention is preferably a solvent capable of isolating the resulting polyimide precursor as a powder, for example, an amide solvent represented by N, N-dimethylformamide or dioxane Water-soluble ethers, water-soluble ketones represented by acetone, and water-soluble alcohols represented by methanol. Among these solvent types, N, N-dimethylformamide, N, N-dimethylacetamide, N-methylpyrrolidone, dioxane, tetrahydrofuran, acetone or methanol are preferable, and a plurality of mixed solvents composed of a combination thereof may be used. .
Furthermore, various other solvents may be mixed with the above solvents and used as a synthesis solvent, as long as the practice of the present invention is not hindered. The temperature in the reaction system does not need to be particularly controlled,
It may be performed at room temperature.

【0022】本発明のポリイミド前駆体粉体は、種々溶
媒に溶解してポリイミド前駆体溶液とし、これを用いて
ポリイミドフィルムやポリイミド塗膜等に成形したり、
またイミド閉環してポリイミド粉体に変換し、成形体に
成形することができる。成形は、公知のように200〜
450℃程度の加熱下、100〜1500kgf/cm
2 程度の条件で加熱圧縮することにより容易に行うこと
ができる。なお、この際、成形時の揮発成分の発生を無
くするため、300℃程度で十分に予備焼成したポリイ
ミド粉体を用いるのが好ましい。なお、イミド閉環はポ
リイミド前駆体粉体を加熱焼成することにより、あるい
は無水酢酸に代表される脱水剤で化学的に処理すること
により進行する。焼成は、例えば、空気中、窒素等の不
活性雰囲気中もしくは真空中で120℃〜250℃の温
度で行うと、ポリイミド前駆体粉体がイミド閉環して高
重合度のポリイミドに変換される。
The polyimide precursor powder of the present invention is dissolved in various solvents to form a polyimide precursor solution, which is used to form a polyimide film or a polyimide coating film,
Further, it can be converted into a polyimide powder by imide ring closure and molded into a molded article. Molding is carried out in a known manner from 200 to
Under heating of about 450 ° C, 100-1500kgf / cm
It can be easily performed by heating and compressing under about 2 conditions. In this case, it is preferable to use polyimide powder which has been sufficiently preliminarily fired at about 300 ° C. in order to eliminate generation of volatile components during molding. The imide ring closure proceeds by heating and baking the polyimide precursor powder or chemically treating it with a dehydrating agent represented by acetic anhydride. For example, when the firing is performed at a temperature of 120 ° C. to 250 ° C. in air, in an inert atmosphere such as nitrogen, or in a vacuum, the polyimide precursor powder undergoes imide ring closure to be converted into a polyimide having a high degree of polymerization.

【0023】また、得られるポリイミドの種々特性を改
善する目的で、無機もしくは有機質フィラーを配合する
場合は、必要量をポリイミド前駆体粉体製造時の反応系
中に添加しておくと均一にフィラーの分散したポリイミ
ド組成物が得られるので、好ましい。
When an inorganic or organic filler is blended for the purpose of improving various properties of the obtained polyimide, a necessary amount of the filler can be uniformly added to the reaction system during the production of the polyimide precursor powder. Is preferable since a polyimide composition in which is dispersed is obtained.

【0024】[0024]

【実施例】以下、実施例により本発明を具体的に説明す
る。なお、実施例中、Tgの測定は、DSC測定装置D
SC−7(Perkin-Elmer社製)を用いて窒素雰囲気中で
行った。また、熱分解開始温度は、TGA測定装置TG
A−7(Perkin-Elmer社製)を用いて窒素雰囲気中で測
定した。ポリイミド前駆体の重合度の測定は、GPC測
定装置を用いて行い、ポリスチレン換算の重量平均分子
量(Mw)で評価した。
The present invention will be described below in detail with reference to examples. In the examples, the Tg was measured using a DSC
This was performed in a nitrogen atmosphere using SC-7 (manufactured by Perkin-Elmer). In addition, the thermal decomposition starting temperature is determined by a TGA measuring device TG.
It measured in nitrogen atmosphere using A-7 (made by Perkin-Elmer). The degree of polymerization of the polyimide precursor was measured using a GPC measuring device, and evaluated by weight average molecular weight (Mw) in terms of polystyrene.

【0025】実施例1 100gのN,N−ジメチルホルムアミド中に100g
(0.279モル)のビフェニルテトラカルボン酸ジメ
チルエステルを溶解し、55.9g(0.279モル)
の4,4’−オキシジアニリンを加え、25℃で12時
間攪拌し、乳白色の懸濁液を得た。これを、100℃で
12時間減圧乾燥し、300μmのメッシュ上で粉砕
し、平均粒子径80μm程度の白色のポリイミド前駆体
粉体148gを得た。得られた粉体のMwは1000以
下であった。得られたポリイミド前駆体粉体を200℃
で16時間減圧加熱したところ、黄色のポリイミド粉体
を得た。このポリイミド粉体におけるTgは285℃で
あり、熱分解開始温度は588℃であった。
Example 1 100 g of N, N-dimethylformamide in 100 g
(0.279 mol) of biphenyltetracarboxylic acid dimethyl ester was dissolved, and 55.9 g (0.279 mol) was dissolved.
Of 4,4′-oxydianiline was added and stirred at 25 ° C. for 12 hours to obtain a milky white suspension. This was dried under reduced pressure at 100 ° C. for 12 hours and pulverized on a 300 μm mesh to obtain 148 g of a white polyimide precursor powder having an average particle diameter of about 80 μm. Mw of the obtained powder was 1,000 or less. The obtained polyimide precursor powder was heated at 200 ° C.
After heating under reduced pressure for 16 hours, a yellow polyimide powder was obtained. The Tg of this polyimide powder was 285 ° C., and the thermal decomposition onset temperature was 588 ° C.

【0026】実施例2 400gのメタノール中に100g(0.279モル)
のビフェニルテトラカルボン酸ジメチルエステルを溶解
し、55.9g(0.279モル)の4,4’−オキシ
ジアニリンを加え20℃で18時間攪拌し、乳白色の懸
濁液を得た。これを、濾別して60℃で12時間減圧乾
燥し、300μmのメッシュ上で粉砕し、平均粒子径5
0μm程度の白色のポリイミド前駆体粉体152gを得
た。得られた粉体のMwは1000以下であった。得ら
れたポリイミド前駆体粉体を200℃で16時間減圧加
熱したところ、黄色のポリイミド粉体を得た。このポリ
イミド粉体におけるTgは282℃であり、熱分解開始
温度は578℃であった。
Example 2 100 g (0.279 mol) in 400 g of methanol
Was dissolved, 55.9 g (0.279 mol) of 4,4′-oxydianiline was added, and the mixture was stirred at 20 ° C. for 18 hours to obtain a milky white suspension. This was separated by filtration, dried under reduced pressure at 60 ° C. for 12 hours, pulverized on a mesh of 300 μm,
152 g of a white polyimide precursor powder of about 0 μm was obtained. Mw of the obtained powder was 1,000 or less. When the obtained polyimide precursor powder was heated under reduced pressure at 200 ° C. for 16 hours, a yellow polyimide powder was obtained. The Tg of this polyimide powder was 282 ° C., and the thermal decomposition onset temperature was 578 ° C.

【0027】実施例3 100gのN,N−ジメチルホルムアミド及び200g
のメタノールからなる混合溶液中に、100g(0.2
79モル)のビフェニルテトラカルボン酸ジメチルエス
テルを溶解し、さらに55.9g(0.279モル)の
4,4’−オキシジアニリンを加え20℃で18時間攪
拌し、白色の懸濁液を得た。これを、濾別して60℃で
12時間減圧乾燥し、300μmのメッシュ上で粉砕
し、平均粒子径80μm程度の白色のポリイミド前駆体
粉体147gを得た。得られた粉体のMwは1000以
下であった。得られたポリイミド前駆体粉体を200℃
で16時間減圧加熱したところ、黄色のポリイミド粉体
を得た。このポリイミド粉体におけるTgは284℃で
あり、熱分解開始温度は578℃であった。
Example 3 100 g of N, N-dimethylformamide and 200 g
100 g (0.2 g) in a mixed solution of methanol
79 mol) of biphenyltetracarboxylic acid dimethyl ester was dissolved, and 55.9 g (0.279 mol) of 4,4′-oxydianiline was further added thereto, followed by stirring at 20 ° C. for 18 hours to obtain a white suspension. Was. This was separated by filtration, dried under reduced pressure at 60 ° C. for 12 hours, and pulverized on a 300 μm mesh to obtain 147 g of a white polyimide precursor powder having an average particle diameter of about 80 μm. Mw of the obtained powder was 1,000 or less. The obtained polyimide precursor powder was heated at 200 ° C.
After heating under reduced pressure for 16 hours, a yellow polyimide powder was obtained. The Tg of this polyimide powder was 284 ° C., and the thermal decomposition onset temperature was 578 ° C.

【0028】比較例1 155.11g(0.5モル)のビフェニルテトラカル
ボン酸二無水物と100.12g(0.5モル)の4,
4’オキシジアニリンを、1500gのN−メチルピロ
リドン中で25℃で3時間撹拌し、粘調な褐色溶液を得
た。得られた溶液のMwは150000であった。この
溶液に、150gの無水酢酸を徐々に撹拌下に添加し、
系全体を140℃で15時間撹拌し、黄色の懸濁液を得
た。これを濾別して200℃で12時間減圧下乾燥し、
ポリイミド粉体を得た。Tgは284℃であり、熱分解
開始温度は578℃であった。
Comparative Example 1 155.11 g (0.5 mol) of biphenyltetracarboxylic dianhydride and 100.12 g (0.5 mol) of 4,
The 4 ′ oxydianiline was stirred in 1500 g of N-methylpyrrolidone at 25 ° C. for 3 hours to obtain a viscous brown solution. Mw of the obtained solution was 150,000. To this solution, 150 g of acetic anhydride was slowly added with stirring,
The whole system was stirred at 140 ° C. for 15 hours to obtain a yellow suspension. This was separated by filtration and dried under reduced pressure at 200 ° C. for 12 hours.
A polyimide powder was obtained. Tg was 284 ° C., and thermal decomposition onset temperature was 578 ° C.

【0029】比較例2 300gのN,N−ジメチルホルムアミド中に100g
(0.3モル)のビフェニルテトラカルボン酸を溶解
し、60.6g(0.3モル)の4,4−オキシジアニ
リンを加え20℃で30分間攪拌し、黄色溶液を得た。
これをトレーに流延し、3時間静置したところ徐々に白
色の析出物が見られ、最終的に懸濁液が得られた。これ
を、80℃で4時間減圧乾燥し、150μmのメッシュ
上で粉砕し、平均粒子径100μm程度の白色のポリイ
ミド前駆体粉体154gを得た。得られた粉体のMwは
1000以下であった。これを濾別して200℃で12
時間減圧下乾燥し、ポリイミド粉体を得た。得られたポ
リイミド粉体におけるTgは284℃であり、熱分解開
始温度は585℃であった。
Comparative Example 2 100 g in 300 g of N, N-dimethylformamide
(0.3 mol) of biphenyltetracarboxylic acid was dissolved, 60.6 g (0.3 mol) of 4,4-oxydianiline was added, and the mixture was stirred at 20 ° C. for 30 minutes to obtain a yellow solution.
This was cast on a tray and allowed to stand for 3 hours, whereupon a white precipitate was gradually observed, and finally a suspension was obtained. This was dried under reduced pressure at 80 ° C. for 4 hours and pulverized on a 150 μm mesh to obtain 154 g of a white polyimide precursor powder having an average particle diameter of about 100 μm. Mw of the obtained powder was 1,000 or less. This is filtered off at 200 ° C. for 12 hours.
After drying under reduced pressure for a time, a polyimide powder was obtained. The Tg of the obtained polyimide powder was 284 ° C., and the thermal decomposition onset temperature was 585 ° C.

【0030】実施例1〜3及び比較例1〜2から、本発
明によるポリイミド前駆体粉体から得られるポリイミド
粉体は、従来法で得られるポリイミド粉体と全く同一の
ものであることがわかった。すなわち、本発明によるポ
リイミド前駆体粉体から得られるポリイミド粉体は、高
重合度のポリイミドからなるものであることがわかっ
た。
Examples 1 to 3 and Comparative Examples 1 and 2 show that the polyimide powder obtained from the polyimide precursor powder according to the present invention is exactly the same as the polyimide powder obtained by the conventional method. Was. That is, it was found that the polyimide powder obtained from the polyimide precursor powder according to the present invention was composed of polyimide having a high degree of polymerization.

【0031】[0031]

【発明の効果】以上ように、本発明の全芳香族ポリイミ
ド前駆体粉体は、低分子量のポリイミド前駆体よりなる
ので、加水分解などがおこりにくく、安定性に優れたも
のであり、高重合度のポリイミド粉体に変換しうる。ま
た、本発明の製造方法によれば、ポリイミド前駆体粉体
を安価に、しかも容易に得ることができる。
As described above, since the wholly aromatic polyimide precursor powder of the present invention is composed of a low molecular weight polyimide precursor, it does not easily undergo hydrolysis and the like, is excellent in stability, and has high polymerization. Degree of polyimide powder. Further, according to the production method of the present invention, the polyimide precursor powder can be easily obtained at low cost.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 越後 良彰 京都府宇治市宇治小桜23番地 ユニチカ株 式会社中央研究所内 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Yoshiaki Echigo 23 Uji Kozakura, Uji City, Kyoto Prefecture Inside Unitika Central Research Laboratory

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 芳香族ジアミンと構造式(1)に示す芳
香族テトラカルボン酸ジエステルとから形成されている
塩からなる全芳香族ポリイミド前駆体粉体。 【化1】 ここでRは炭素数1〜5のアルキル基を示す。
1. A wholly aromatic polyimide precursor powder comprising a salt formed from an aromatic diamine and an aromatic tetracarboxylic acid diester represented by the structural formula (1). Embedded image Here, R represents an alkyl group having 1 to 5 carbon atoms.
【請求項2】 芳香族ジアミンと構造式(1)に示す芳
香族テトラカルボン酸ジエステルとを溶媒中で混合して
塩を形成させて、溶媒を除去して単離することを特徴と
する全芳香族ポリイミド前駆体粉体の製造方法。 【化2】
2. A method comprising mixing an aromatic diamine and an aromatic tetracarboxylic acid diester represented by the structural formula (1) in a solvent to form a salt, removing the solvent and isolating the salt. A method for producing an aromatic polyimide precursor powder. Embedded image
JP34262697A 1997-12-12 1997-12-12 Wholly aromatic polyimide precursor powder and its production Pending JPH11171990A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34262697A JPH11171990A (en) 1997-12-12 1997-12-12 Wholly aromatic polyimide precursor powder and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34262697A JPH11171990A (en) 1997-12-12 1997-12-12 Wholly aromatic polyimide precursor powder and its production

Publications (1)

Publication Number Publication Date
JPH11171990A true JPH11171990A (en) 1999-06-29

Family

ID=18355236

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34262697A Pending JPH11171990A (en) 1997-12-12 1997-12-12 Wholly aromatic polyimide precursor powder and its production

Country Status (1)

Country Link
JP (1) JPH11171990A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007112926A (en) * 2005-10-21 2007-05-10 Toyobo Co Ltd Polyimide precursor powder
JP2007112927A (en) * 2005-10-21 2007-05-10 Toyobo Co Ltd Polyimide resin powder and method for producing polyimide resin molding

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007112926A (en) * 2005-10-21 2007-05-10 Toyobo Co Ltd Polyimide precursor powder
JP2007112927A (en) * 2005-10-21 2007-05-10 Toyobo Co Ltd Polyimide resin powder and method for producing polyimide resin molding

Similar Documents

Publication Publication Date Title
JP5281340B2 (en) Oxidation stable hard aromatic polyimide composition
US9334368B2 (en) Polyimide precursor solution composition
JP4947989B2 (en) Polyimide precursor solution, polyimide porous film, and production method thereof
US5116939A (en) Polyimide processing additives
JP2008101186A (en) Amino acid ester oligomer, precursor composition for polyimide resin containing it, and use
JP7020704B2 (en) Polyimide-based copolymer and polyimide-based film containing it
JP3513951B2 (en) Polyamideimide resin and adhesive and coating agent containing the same
JPH11171990A (en) Wholly aromatic polyimide precursor powder and its production
US5504182A (en) Thermoplastically processable aromatic polyether amide
JPH11140185A (en) Wholly aromatic polyimide precursor powder and its production
JP6483481B2 (en) Torxic acid based polymer and its production intermediate
US5272248A (en) Polyimide processing additives
JPH04227635A (en) Production of aromatic polyamide-polyimide copolymer
JPH05230211A (en) Polyimide resin
JP2860987B2 (en) Method for producing polyimide powder
JP2900367B2 (en) Polyamic acid solution and method for producing powder of polyimide
JPH08120077A (en) Production of polyimide precursor powder
JPH1135683A (en) Wholly aromatic polyimide precursor powder and its production
JPH01201335A (en) Polyamide-polyimide block copolymer
JPH11302377A (en) Production of polyimide powdery material
JP2862173B2 (en) Method for producing polyimide powder composition
JPH01149830A (en) Thermoplastic aromatic polyimide polymer
JP2000176264A (en) Fluid separation membrane made of polyether imide
JPH09188760A (en) Production of polyisoimide solution
JP2000001545A (en) Production of polyimide powder