JPH11140185A - Wholly aromatic polyimide precursor powder and its production - Google Patents

Wholly aromatic polyimide precursor powder and its production

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Publication number
JPH11140185A
JPH11140185A JP30677897A JP30677897A JPH11140185A JP H11140185 A JPH11140185 A JP H11140185A JP 30677897 A JP30677897 A JP 30677897A JP 30677897 A JP30677897 A JP 30677897A JP H11140185 A JPH11140185 A JP H11140185A
Authority
JP
Japan
Prior art keywords
polyimide precursor
polyimide
powder
precursor powder
wholly 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
JP30677897A
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 JP30677897A priority Critical patent/JPH11140185A/en
Publication of JPH11140185A publication Critical patent/JPH11140185A/en
Pending legal-status Critical Current

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  • Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a polyimide precursor powder comprising a polyimide precursor excellent in stability and convertible into a polyimide of a high degree of polymerization and to provide a process for producing the polyamide precursor powder inexpensively and easily without using a larger amount of a solvent. SOLUTION: This wholly aromatic polyimide precursor powder comprises a salt formed from an aromatic diamine and 3,3',4,4'-biphenyltetracarboxylic acid. An aromatic diamine is mixed with 3,3',4,4'-biphenyltetracarboxylic acid in a poor solvent for the polyimide precursor to be formed to obtain a suspension in which polyimide precursor particles are dispersed, and the polyimide precursor particles are isolated to obtain a wholly aromatic polyimide precursor powder.

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ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention 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。
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.

【0003】一般に、全芳香族ポリイミドは熱軟化点を
有さず、また、溶剤に不溶であるので、成形が困難であ
ることが多く、このため、これら問題を改善する目的で
種々の検討がおこなわれてきた。例えば、多くの場合、
ポリイミドの前駆体であり、アミド結合を有するポリア
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。
Generally, a wholly aromatic polyimide does not have a thermal softening point and is insoluble in a solvent, so that molding is often difficult. Therefore, various studies have been made to improve these problems. It has been done. For example, in many cases
A method of forming a polyamic acid (polymer) having an amide bond, which is a precursor of a polyimide, and converting this into a polyimide has been performed.

【0004】ポリイミド前駆体粉体を得る方法として、
第一の方法としては、ポリイミド前駆体溶液(ポリアミ
ド酸溶液)を貧溶媒に添加して混合し、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1−2920
35号公報、特開平4−272934号公報もしくは特
開平4−272936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。
As a method of obtaining a polyimide precursor powder,
As a first method, a method in which a polyimide precursor solution (polyamic acid solution) is added to a poor solvent and mixed to precipitate a dissolved polyimide precursor is disclosed in JP-A-1-2920.
No. 35, JP-A-4-272934 or JP-A-4-272936. 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 is required for polyamic acid, and the polyamic acid solution and the poor solvent are not used. Has to be strictly controlled. In addition, the degree of polymerization of polyamic acid tends to decrease due to hydrolysis, and care must be taken in its handling.

【0005】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.

【0006】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。
Japanese Patent Publication No. 2-48571 discloses that
In the poor solvent of the resulting polyimide, the monomer component consisting of aromatic tetracaronic dianhydride and the 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 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.

【0007】[0007]

【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.

【0008】[0008]

【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、特定溶媒中で芳香
族ジアミンと特定の芳香族テトラカルボン酸を混合する
と、ポリイミド前駆体粒子の懸濁液が得られ、この懸濁
液からポリイミド前駆体粒子を単離してポリイミド前駆
体粉体を得、これをイミド化処理すると高重合度のポリ
イミド粉体が得られるという知見を得、かかる知見に基
づき、本発明に到達した。
The present inventors have conducted intensive studies to solve the above-mentioned problems. As a result, when an aromatic diamine and a specific aromatic tetracarboxylic acid are mixed in a specific solvent, polyimide precursor particles are obtained. A suspension of is obtained, polyimide precursor particles are isolated from this suspension to obtain a polyimide precursor powder, and the knowledge that a polyimide powder having a high degree of polymerization can be obtained by imidizing the polyimide precursor powder, Based on such findings, the present invention has been achieved.

【0009】すなわち、本発明の要旨は、第一に、芳香
族ジアミンと3,3’,4,4’−ビフェニルテトラカ
ルボン酸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る。第二に、生成するポリイミド
前駆体の貧溶媒中で、芳香族ジアミンと3,3’,4,
4’−ビフェニルテトラカルボン酸とを混合して、ポリ
イミド前駆体粒子が分散している懸濁液を得、ポリイミ
ド前駆体粒子を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。
That is, the gist of the present invention is to provide a wholly aromatic polyimide precursor powder comprising a salt formed of an aromatic diamine and 3,3 ', 4,4'-biphenyltetracarboxylic acid. It is. Second, aromatic diamine and 3,3 ', 4,4
4′-biphenyltetracarboxylic acid is mixed to obtain a suspension in which the polyimide precursor particles are dispersed, and the polyimide precursor particles are isolated to obtain a wholly aromatic polyimide precursor powder. It is a manufacturing method.

【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、3,3’,4,4’−ビフェニルテトラカルボン
酸(以下芳香族テトラカルボン酸と記すことがある)と
から形成される塩からなる粉体である。本発明における
ポリイミド前駆体は、イミド閉環すると下記式(1)に
示す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 is a powder comprising a salt formed from an aromatic diamine and 3,3 ′, 4,4′-biphenyltetracarboxylic acid (hereinafter sometimes referred to as aromatic tetracarboxylic acid). Body. The polyimide precursor in the present invention produces a polyimide comprising a repeating unit represented by the following formula (1) upon imide ring closure. Here, imide ring closure refers to the formation of an imide ring by a thermal or chemical reaction.

【0011】[0011]

【化1】 Embedded image

【0012】上記式(1)において、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し、Rのも
ととなる芳香族ジアミンとしては、下記構造式群に示す
ものが挙げられ、これらのうちの1種、もしくはこれら
の中から選ばれる複数種を用いることができる。
In the above formula (1), R is at least 1
A divalent aromatic residue having two carbon 6-membered rings is shown. Examples of the aromatic diamine as a source of R include those shown in the following structural formula group, and one of these or one of these A plurality of types selected from among them can be used.

【0013】[0013]

【化2】 Embedded image

【0014】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)に示されるように酸と
アミンとの間にアミド結合を有した繰り返し単位からな
るポリマーであるのに対して、本発明におけるポリイミ
ド前駆体は、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)を有する塩である。
The polyamic acid, which is a typical polyimide precursor, is a polymer comprising a repeating unit having an amide bond between an acid and an amine as shown in the following general formula (2). The polyimide precursor in the present invention is a salt having no amide bond and having a weak interaction (ionic bond) between an acid and an amine.

【0015】[0015]

【化3】 Embedded image

【0016】したがって、本発明の全芳香族ポリイミド
前駆体粉体を溶解する種々の溶媒中に本発明の全芳香族
ポリイミド前駆体粉体を溶解しても、ただ単にモノマー
が塩を形成し、これが分散している状態の液であること
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ことはない。
Therefore, even if the wholly aromatic polyimide precursor powder of the present invention is dissolved in various solvents for dissolving the wholly aromatic polyimide precursor powder of the present invention, the monomer simply forms a salt, Since this is a liquid in a dispersed state, the viscosity of the solution does not suddenly increase as the concentration or the degree of polymerization increases unlike a polymer solution.

【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 are substantially equimolar, that is, 0.9 to 1.1 moles of the aromatic tetracarboxylic acid per mole of the aromatic diamine. It is preferably formed from moles. 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、生成す
るポリイミド前駆体の貧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を
混合すると、ポリイミド前駆体粒子が分散した懸濁液が
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ので好ましい。
また、このとき、懸濁液中のポリイミド前駆体粒子の分
散濃度は5〜50重量%となるようにすることが好まし
い。懸濁液中のポリイミド前駆体粒子が5重量%未満で
は生産性に欠け、50重量%を越えると懸濁液の流動性
が悪くなり、均一に混合できないなど取扱いに劣る傾向
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 in a poor solvent for the resulting polyimide precursor.
When approximately equimolar amounts of an aromatic diamine and an aromatic tetracarboxylic acid are mixed, a suspension in which polyimide precursor particles are dispersed is obtained. At this time, the aromatic diamine and the aromatic tetracarboxylic acid may be directly added to the reaction system, 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 acid is not particularly limited, but it is preferable to add the aromatic diamine to a system in which the aromatic tetracarboxylic acid is dissolved or dispersed in a solvent, because the mixture can be uniformly mixed in a short time.
At this time, it is preferable that the dispersion concentration of the polyimide precursor particles in the suspension is 5 to 50% by weight. If the amount of the polyimide precursor particles in the suspension is less than 5% by weight, the productivity is poor, and if it exceeds 50% by weight, the fluidity of the suspension is deteriorated, and the suspension tends to be inferior in handling, such as being unable to mix uniformly.

【0019】本発明において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の貧溶
媒であればいかなるものでも用いることができるが、好
ましいものとして、N,N−ジメチルホルムアミド、水
溶性アルコール等が挙げられ、これらの溶媒は単独で、
あるいはこれらの溶媒を組み合わせて用いることができ
る。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反応溶媒として用いても
差し支えない。
In the present invention, any solvent may be used as a solvent for producing the polyimide precursor powder, as long as it is a poor solvent for the polyimide precursor to be produced. Preferred examples include N, N-dimethylformamide, Alcohols and the like, and these solvents are used alone,
Alternatively, these solvents can be used in combination. Furthermore, various other solvents may be mixed with the above solvents and used as a reaction solvent within a range not to hinder the practice of the present invention.

【0020】前記水溶性アルコールとしては、例えば、
メチルアルコール、エチルアルコール、イソプロピルア
ルコール、n−プロピルアルコール、1,2−エタンジ
オール、1,2−プロパンジオール、1,3−プロパン
ジオール、1,3−ブタンジオール、1,4−ブタンジ
オール、2,3−ブタンジオール、1,5−ペンタンジ
オール、2−ブテン−1,4−ジオール、2−メチル−
2,4−ペンタンジオール、グリセリン、2−エチル−
2−(ヒドロキシメチル)−1,3−プロパンジオー
ル、1,2,6−ヘキサントリオールなどが挙げられ
る。これら溶媒のうち、特に好ましくはメチルアルコー
ルである。
Examples of the water-soluble alcohol include, for example,
Methyl alcohol, ethyl alcohol, isopropyl alcohol, n-propyl alcohol, 1,2-ethanediol, 1,2-propanediol, 1,3-propanediol, 1,3-butanediol, 1,4-butanediol, , 3-butanediol, 1,5-pentanediol, 2-butene-1,4-diol, 2-methyl-
2,4-pentanediol, glycerin, 2-ethyl-
2- (hydroxymethyl) -1,3-propanediol, 1,2,6-hexanetriol and the like. Among these solvents, methyl alcohol is particularly preferred.

【0021】反応系中の温度は特に制御する必要はな
く、常温でよい。なお、N,N−ジメチルホルムアミド
を貧溶媒として使用する場合、反応系の温度は50℃以
下が好ましく、特に好ましくは30℃以下である。反応
系の温度が50℃を越えると、生成するポリイミド前駆
体の収量が著しく減少し、収率が悪くなる傾向にあるた
め好ましくない。
The temperature in the reaction system does not need to be particularly controlled, and may be room temperature. When N, N-dimethylformamide is used as a poor solvent, the temperature of the reaction system is preferably 50 ° C. or lower, particularly preferably 30 ° C. or lower. If the temperature of the reaction system exceeds 50 ° C., the yield of the polyimide precursor to be produced is remarkably reduced, and the yield tends to deteriorate, which is not preferable.

【0022】ポリイミド前駆体粒子が分散している懸濁
液からは、濾過もしくは乾燥により容易に溶媒を除去で
き、粒径5〜150μmのポリイミド前駆体粉体を単離
することができる。また、懸濁液を例えば0.5〜3倍
量の水やトルエン、ヘキサメチレンなどに添加し、一部
貧溶媒中に溶解しているポリイミド前駆体を析出させる
ことにより、より高収量のポリイミド前駆体粉体を得る
ことができる。
From the suspension in which the polyimide precursor particles are dispersed, the solvent can be easily removed by filtration or drying, and a polyimide precursor powder having a particle size of 5 to 150 μm can be isolated. Further, by adding the suspension to, for example, 0.5 to 3 times the amount of water, toluene, hexamethylene, etc., and precipitating a polyimide precursor partially dissolved in a poor solvent, a higher yield of polyimide is obtained. A precursor powder can be obtained.

【0023】本発明のポリイミド前駆体粉体は、ポリイ
ミド前駆体を溶解する種々溶媒に溶解してポリイミド前
駆体溶液とし、この溶液からポリイミドフィルムやポリ
イミド塗膜等を成形したり、また、ポリイミド前駆体粉
体をイミド閉環してポリイミド粉体に変換し、これを成
形して成形体にすることができる。成形条件は、公知条
件例えば200〜450℃、100〜1500kgf/
cm2 で、加熱圧縮することにより、容易に成形するこ
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。
The polyimide precursor powder of the present invention is dissolved in various solvents for dissolving the polyimide precursor to form a polyimide precursor solution, from which a polyimide film or a polyimide coating film is formed. The body powder can be converted into a polyimide powder by imide ring closure and then molded to form a compact. Molding conditions are known conditions, for example, 200 to 450 ° C., 100 to 1500 kgf /
It can be easily molded by heating and compressing at cm 2 . 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.

【0024】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 imide ring closure proceeds by heating and firing the polyimide precursor powder or by 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.

【0025】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 the various properties of the obtained polyimide, a necessary amount of the filler is uniformly added to the reaction system at the time of producing the polyimide precursor powder. Is preferable since a polyimide composition in which is dispersed is obtained.

【0026】[0026]

【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 TTGA−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
It carried out in nitrogen atmosphere using SC-7 (made by Perkin-Elmer). In addition, the thermal decomposition onset temperature
The measurement was performed in a nitrogen atmosphere using a measuring device TTGA-7 (manufactured 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.

【0027】実施例1 2500gのメタノール中に溶解した495.3g
(1.5モル)の3,3’,4,4’−ビフェニルテト
ラカルボン酸に、300.4g(1.5モル)の4,
4’−オキシジアニリンを加え25℃で12時間攪拌
し、白色の懸濁液を得た。これを、濾別して60℃で1
2時間減圧乾燥し、150μm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
725g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1
6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のTgは285℃であり、熱分
解開始温度は592℃であり、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、本発明の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ことがわ
かる。
Example 1 495.3 g dissolved in 2500 g of methanol
(1.5 mol) of 3,3 ′, 4,4′-biphenyltetracarboxylic acid was added to 300.4 g (1.5 mol) of 4,
4′-Oxydianiline was added and the mixture was stirred at 25 ° C. for 12 hours to obtain a white suspension. This is filtered off at 60 ° C. for 1 hour.
Dry under reduced pressure for 2 hours, pulverize on a 150 μm mesh,
725 g of a white polyimide precursor powder having an average particle diameter of about 80 μm was obtained. Mw of the obtained powder was 1,000 or less. The obtained polyimide precursor powder is heated at 200 ° C. for 1 hour.
After heating under reduced pressure for 6 hours, a yellow polyimide powder was obtained. The Tg of this polyimide powder was 285 ° C., and the thermal decomposition onset temperature was 592 ° C., which proved to be exactly the same as the polyimide powder obtained by the conventional method. That is, it is understood that the polyimide powder obtained from the polyimide precursor powder of the present invention is composed of a polyimide having a high degree of polymerization.

【0028】実施例2 1500gのN,N−ジメチルホルムアミド中に溶解し
た495.3g(1.5モル)の3,3’,4,4’−
ビフェニルテトラカルボン酸に、300.4g(1.5
モル)の44’−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、500gの
純水中に添加しさらに20℃で3時間撹拌し、濾別して
60℃で12時間減圧乾燥し、150μm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730gを得た。得られた粉体のMwは10
00以下であった。得られたポリイミド前駆体粉体を2
00℃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のTgは278℃で
あり、熱分解開始温度は579℃であり、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、本発明の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
ることがわかる。
Example 2 495.3 g (1.5 mol) of 3,3 ', 4,4'- dissolved in 1500 g of N, N-dimethylformamide
To biphenyltetracarboxylic acid, 300.4 g (1.5
Mol) of 44'-oxydianiline, and
After stirring for an hour, a white suspension was obtained. This was added to 500 g of pure water, further stirred at 20 ° C. for 3 hours, filtered, dried at 60 ° C. under reduced pressure for 12 hours, pulverized on a 150 μm mesh, and a white polyimide precursor having an average particle diameter of about 80 μm. 730 g of powder was obtained. Mw of the obtained powder is 10
00 or less. The obtained polyimide precursor powder was mixed with 2
When heated under reduced pressure at 00 ° C. for 16 hours, a yellow polyimide powder was obtained. The Tg of this polyimide powder was 278 ° C., and the thermal decomposition onset temperature was 579 ° C., which proved to be exactly the same as the polyimide powder obtained by the conventional method. That is, it is understood that the polyimide powder obtained from the polyimide precursor powder of the present invention is composed of a polyimide having a high degree of polymerization.

【0029】実施例3 500gのN,N−ジメチルホルムアミド及び1000
gのメタノールからなる混合溶液中に溶解した495.
3g(1.5モル)の3,3’,4,4’−ビフェニル
テトラカルボン酸に、300.4g(1.5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、150μm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750g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のTgは285℃であり、
熱分解開始温度は581℃であり、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、本発明の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こと
がわかる。
Example 3 500 g of N, N-dimethylformamide and 1000 g
495 dissolved in a mixed solution consisting of methanol.
To 3 g (1.5 mol) of 3,3 ′, 4,4′-biphenyltetracarboxylic acid, 300.4 g (1.5 mol) of 4,4′-oxydianiline was added and stirred at 20 ° C. for 18 hours. To give a white suspension. This was filtered, dried under reduced pressure at 60 ° C. for 12 hours, and pulverized on a 150 μm mesh to obtain 750 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 is 285 ° C.,
The thermal decomposition onset temperature was 581 ° C., which was found to be exactly the same as the polyimide powder obtained by the conventional method.
That is, it is understood that the polyimide powder obtained from the polyimide precursor powder of the present invention is composed of a polyimide having a high degree of polymerization.

【0030】実施例4 300gのN,N−ジメチルホルムアミド中に溶解した
100.0g(0.3モル)の3,3’,4,4’−ビ
フェニルテトラカルボン酸に、60.6g(0.3モ
ル)の4,4’−オキシジアニリンを加え20℃で30
粉間攪拌し、黄色の溶液を得た。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15
4gを得た。得られた粉体のMwは1000以下であっ
た。
Example 4 60.6 g (0.10 g) was added to 100.0 g (0.3 mol) of 3,3 ', 4,4'-biphenyltetracarboxylic acid dissolved in 300 g of N, N-dimethylformamide. 3 mol) of 4,4'-oxydianiline and added at 20 ° C.
Stirring between the powders gave 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 a white polyimide precursor powder 15 having an average particle diameter of about 100 μm.
4 g were obtained. Mw of the obtained powder was 1,000 or less.

【0031】比較例1 155.11g(0.5モル)の4,4’−オキシジフ
タル酸二無水物と1 00.12g(0.5モル)の3,
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添加し、
系全体を140℃で15時間撹拌し、黄褐色の懸濁液を
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。得られたポリイミド粉体の
Tgは280℃であった。また、熱分解開始温度は、5
85℃であった。
Comparative Example 1 155.11 g (0.5 mol) of 4,4'-oxydiphthalic dianhydride and 100.12 g (0.5 mol) of 3,4
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 gradually added under stirring,
The whole system was stirred at 140 ° C. for 15 hours to obtain a tan suspension. This was separated by filtration and dried under reduced pressure at 200 ° C. for 12 hours to obtain a polyimide powder. The Tg of the obtained polyimide powder was 280 ° C. The thermal decomposition onset temperature is 5
85 ° C.

【0032】参考例 実施例1、実施例3及び実施例4で得られたポリイミド
粉体300gを12×12cmの金型中に充填し、30
0℃で3時間減圧した後、金型温度を400℃に昇温
し、充填したポリイミド粉体に200kgf/cm2
圧力をかけ、1時間加熱加圧を保持した後冷却し、黄色
のポリイミド成形体を得た。得られた成形体を所定の形
状に切削加工し、表に記載の各特性値を得た。なお各特
性値はJIS規格に準じて測定した。
Reference Example 300 g of the polyimide powder obtained in Examples 1, 3 and 4 was filled in a mold of 12 × 12 cm.
After reducing the pressure at 0 ° C. for 3 hours, the mold temperature was raised to 400 ° C., a pressure of 200 kgf / cm 2 was applied to the filled polyimide powder, the heating and pressurizing was maintained for 1 hour, and then cooling was performed. A molded article was obtained. The obtained molded body was cut into a predetermined shape to obtain each characteristic value shown in the table. In addition, each characteristic value was measured according to JIS standard.

【0033】[0033]

【表1】 [Table 1]

【0034】[0034]

【発明の効果】以上のように、本発明のポリイミド前駆
体粉体は、安定性に優れ、高重合度のポリイミドに変換
しうる。しかも、本発明の製造方法によればこのような
ポリイミド前駆体粉体を多量の溶媒を用いることなく安
価に、しかも容易に提供することができる。
As described above, the polyimide precursor powder of the present invention has excellent stability and can be converted to a polyimide having a high degree of polymerization. Moreover, according to the production method of the present invention, such a polyimide precursor powder can be easily provided at low cost without using a large amount of solvent.

───────────────────────────────────────────────────── 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 (5)

【特許請求の範囲】[Claims] 【請求項1】 芳香族ジアミンと3,3’,4,4’−
ビフェニルテトラカルボン酸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。
1. An aromatic diamine and 3,3 ′, 4,4′-
A wholly aromatic polyimide precursor powder comprising a salt formed with biphenyltetracarboxylic acid.
【請求項2】 生成する全芳香族ポリイミド前駆体の貧
溶媒中で、芳香族ジアミンと3,3’,4,4’−ビフ
ェニルテトラカルボン酸とを混合して、ポリイミド前駆
体粒子が分散している懸濁液を得、ポリイミド前駆体粒
子を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。
2. An aromatic diamine and 3,3 ′, 4,4′-biphenyltetracarboxylic acid are mixed in a poor solvent for a wholly aromatic polyimide precursor to be produced to disperse polyimide precursor particles. A method for producing a wholly aromatic polyimide precursor powder, comprising obtaining a suspension and isolating polyimide precursor particles.
【請求項3】 貧溶媒がN,N−ジメチルホルムアミド
である請求項2記載の全芳香族ポリイミド前駆体粉体の
製造方法。
3. The method for producing a wholly aromatic polyimide precursor powder according to claim 2, wherein the poor solvent is N, N-dimethylformamide.
【請求項4】 貧溶媒が水溶性アルコールである請求項
2記載の全芳香族ポリイミド前駆体粉体の製造方法。
4. The method for producing a wholly aromatic polyimide precursor powder according to claim 2, wherein the poor solvent is a water-soluble alcohol.
【請求項5】 貧溶媒がN,N−ジメチルホルムアミド
及び水溶性アルコールの混合溶液である請求項2記載の
全芳香族ポリイミド前駆体粉体の製造方法。
5. The method for producing a wholly aromatic polyimide precursor powder according to claim 2, wherein the poor solvent is a mixed solution of N, N-dimethylformamide and a water-soluble alcohol.
JP30677897A 1997-11-10 1997-11-10 Wholly aromatic polyimide precursor powder and its production Pending JPH11140185A (en)

Priority Applications (1)

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Publication Number Publication Date
JPH11140185A true JPH11140185A (en) 1999-05-25

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ID=17961160

Family Applications (1)

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Country Status (1)

Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004055096A1 (en) * 2002-12-16 2004-07-01 Japan Science And Technology Corporation Process for producing fine porous polyimide particle
JP2007112926A (en) * 2005-10-21 2007-05-10 Toyobo Co Ltd Polyimide precursor powder
JP2019147970A (en) * 2014-03-03 2019-09-05 ユニチカ株式会社 Polyimide precursor for solid phase polymerization

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004055096A1 (en) * 2002-12-16 2004-07-01 Japan Science And Technology Corporation Process for producing fine porous polyimide particle
JP2004196869A (en) * 2002-12-16 2004-07-15 Japan Science & Technology Agency Method for producing porous polyimide-based fine particles
JP2007112926A (en) * 2005-10-21 2007-05-10 Toyobo Co Ltd Polyimide precursor powder
JP2019147970A (en) * 2014-03-03 2019-09-05 ユニチカ株式会社 Polyimide precursor for solid phase polymerization

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