JPH0479821B2 - - Google Patents

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Publication number
JPH0479821B2
JPH0479821B2 JP29477686A JP29477686A JPH0479821B2 JP H0479821 B2 JPH0479821 B2 JP H0479821B2 JP 29477686 A JP29477686 A JP 29477686A JP 29477686 A JP29477686 A JP 29477686A JP H0479821 B2 JPH0479821 B2 JP H0479821B2
Authority
JP
Japan
Prior art keywords
solvent
aromatic
polyimide
stretched
mol
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.)
Expired - Lifetime
Application number
JP29477686A
Other languages
Japanese (ja)
Other versions
JPS63147626A (en
Inventor
Kyoichi Matsumoto
Hiroshi Inoe
Tetsuharu Hirano
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.)
Ube Corp
Original Assignee
Ube Industries 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 Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP29477686A priority Critical patent/JPS63147626A/en
Publication of JPS63147626A publication Critical patent/JPS63147626A/en
Publication of JPH0479821B2 publication Critical patent/JPH0479821B2/ja
Granted legal-status Critical Current

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  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Moulding By Coating Moulds (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
  • Artificial Filaments (AREA)

Description

【発明の詳现な説明】[Detailed description of the invention]

〔産業䞊の利甚分野〕 この発明は、特定の耐熱性の芳銙族ポリむミド
からなり、極めお優れた物性、特に高いダング率
を有する新芏な延䌞成圢䜓䟋えばフむルム、繊
維など、および、その延䌞成圢䜓の新芏な補造
法に関するものである。 この発明のポリむミド延䌞成圢䜓は、通垞の溶
液流延法で成圢したこの皮の芳銙族ポリむミドフ
むルムなどず比范しお高いレベルの匕匵匷床、耐
熱性などず共に、高いダング率を有しおいるの
で、特に、薄いフむルムたたは现い繊維ずしお
も、皮々の甚途に充分に䜿甚するこずができる。 〔埓来技術〕 埓来、熱収瞮性を有する芳銙族ポリむミドフむ
ルム延䌞フむルムを補造する方法ずしおは、
䟋えば、特公昭57−41330号公報に蚘茉されおい
るように、ビプニルテトラカルボン酞系の芳銙
族ポリむミド前躯䜓ポリアミツク酞、たたはポ
リアミド酞の溶液を20〜200℃の枩床に保ち流
延法で補膜し、そしお200〜500℃の枩床に加熱し
お揮発分含有量が10重量以䞋になるたで也燥さ
せお埗られるポリアミツク酞の少くずも50重量
がポリむミドに転化したポリむミドフむルムを
埗、その埌該ポリむミドフむルムを少くずも方
向に延䌞倍率が1.05〜倍になるように100〜500
℃の枩床で延䌞する方法が、提案されおいる。 しかし、前蚘の方法では、熱収瞮性を有するポ
リむミドフむルムを補造するこずが䞀応できるけ
れども、溶媒の含有率の䜎い『むミド化率の高い
未延䌞フむルム』を無理に延䌞するため、たたは
むミド化および延䌞ずが同時に行われるので、安
定的に延䌞操䜜を行うこずが困難であり、たた、
高いダング率などの物性を有するポリむミド延䌞
フむルムを再珟性よく補造するこずは、困難であ
るか、或いは実質的にできなか぀た。 〔本発明で解決しようずする課題〕 この発明の目的は、芳銙族ポリむミド成圢䜓が
本来有しおいる優れた耐熱性を保持したたた、匕
匵匷床などがより高いず共に、高いダング率を有
する高物性の新芏な芳銙族ポリむミド延䌞成圢䜓
䟋えば、フむルム、繊維などを提䟛するこず
であり、たた、そのような高物性の芳銙族ポリむ
ミド延䌞成圢䜓を工業的に再珟性よく補造するこ
ずができる方法を提䟛するこずである。 〔本発明の芁件〕 すなわち、この発明は、ビプニルテトラカル
ボン酞類を80モル以䞊含有する芳銙族テトラカ
ルボン酞成分ず、ゞアミノゞプニル゚ヌテル類
を70モル以䞊含有する芳銙族ゞアミン成分ずか
ら埗られた芳銙族ポリむミドからなり、しかも、
匕匵匷床ASTM D882が30〜100Kgmm2であ
るず共に、ダング率匕匵匟性率ASTM
D882が400〜800Kgmm2であるポリむミド延䌞
成圢䜓に関するものである。 たた、この発明の補造法は、前述の芳銙族テト
ラカルボン酞成分ず芳銙族ゞアミン成分ずをハロ
ゲン化プノヌル溶媒䞭で重合しお埗られた可溶
性の芳銙族ポリむミドず、50重量以䞋の含有率
のハロゲン化プノヌル溶媒ずからなる未延䌞成
圢䜓を、前蚘ハロゲン化プノヌル溶媒ず盞溶性
であるず共に前蚘芳銙族ポリむミドを実質的に溶
解しない膚最溶媒䞭で充分に膚最させた埌、 膚最した未延䌞成圢䜓を、前蚘の膚最溶媒䞭、
〜200℃の延䌞枩床で、1.1〜3.0倍に延䌞し、 最埌に、その延䌞成圢䜓から溶媒を陀去するず
共に延䌞成圢䜓を熱凊理するこずを特城ずするポ
リむミド延䌞成圢䜓の補造法に関する。 前蚘の芳銙族テトラカルボン酞成分は、䟋え
ば、3′4′−ビプニルテトラカルボン
酞たたはその酞二無氎物、あるいはその酞の炭玠
数〜の䜎玚アルコヌル゚ステル化物、
3′4′−ビプニルテトラカルボン酞たたは
その酞二無氎物、あるいはその酞の炭玠数〜
の䜎玚アルコヌル゚ステル化物などのビプニル
テトラカルボン酞類を、党テトラカルボン酞成分
に察しお、80モル以䞊、特に85モル以䞊含有
する芳銙族テトラカルボン酞成分である。この発
明では、テトラカルボン酞成分ずしお、特に、
3′4′−ビプニルテトラカルボン酞た
たはその酞二無氎物を80モル以䞊、曎に奜たし
くは85モル以䞊含有する芳銙族テトラカルボン
酞成分が、埗られる芳銙族ポリむミドのハロゲン
化プノヌルぞの溶解性、および、最終的に埗ら
れるポリむミド延䌞成圢䜓の成圢性、䞊びに、延
䌞成圢䜓の耐熱性、機械的物性などの点においお
優れおいるので最適である。 なお、前蚘の芳銙族テトラカルボン酞成分は、
ビプニルテトラカルボン酞類の他に、䜵甚する
こずができるテトラカルボン酞類ずしおは、ピロ
メリツト酞たたはその酞二無氎物、ベンゟプノ
ンテトラカルボン酞たたはその酞二無氎物、ビス
−ゞカルボキシプニルメタンたたは
その酞二無氎物、−ビス−ゞカル
ボキシプニルプロパンたたはその酞二無氎
物、ビス−ゞカルボキシプニルスル
ホンたたはその酞二無氎物などを挙げるこずがで
きる。 前蚘の芳銙族ゞアミン成分は、4′−ゞアミ
ノゞプニル゚ヌテル、4′−ゞアミノゞプ
ニル゚ヌテル、3′−ゞアミノゞプニル゚ヌ
テルなどのゞアミノゞプニル゚ヌテル類を、党
芳銙族ゞアミン成分に察しお、70モル以䞊、特
に80モル以䞊、さらに奜たしくは90モル以䞊
含有する芳銙族ゞアミン成分である。この発明で
は、芳銙族ゞアミン成分ずしお、特に、4′−
ゞアミノゞプニル゚ヌテルを70モル以䞊、特
に80モル以䞊の含有率で含有する芳銙族ゞアミ
ン成分が最適である。 なお、前蚘の芳銙族ゞアミン成分においお、ゞ
アミノゞプニル゚ヌテル類の他に、䜵甚するこ
ずができる芳銙族ゞアミン類ずしおは、䟋えば、
4′−ゞアミノゞプニルメタン、4′−ゞ
アミノゞプニルプロパン、4′−ゞアミノゞ
プニルスルホン、4′−ゞアミノゞプニル
スルフむド、−、−たたは−プニレンゞ
アミンなどを挙げるこずができる。 この発明では、前蚘の芳銙族ポリむミドを補造
するための芳銙族ゞアミン成分に぀いお、ゞアミ
ノゞプニル゚ヌテル類の含有率が䜎くなり過ぎ
るず、そのような芳銙族ゞアミン成分ず芳銙族テ
トラカルボン酞成分ずから埗られる芳銙族ポリむ
ミドがハロゲン化プノヌルぞの溶解性が䜎䞋
し、安定に未延䌞成圢䜓を補造するこずができな
いこずがあり適圓ではなく、たた、そのようなポ
リむミドの未延䌞成圢䜓を、延䌞しおも、耐熱
性、前述の各機械的物性のいずれかが䜎䞋した延
䌞成圢䜓しか埗られないので、適圓ではない。 この発明のポリむミド延䌞成圢䜓は、特に、前
述のビプニルテトラカルボン酞類を䞻成分含
有率90モル以䞊ずする芳銙族テトラカルボン酞
成分ず、ゞアミノゞプニル゚ヌテル類を䞻成分
含有率80モル以䞊ずする芳銙族ゞアミン成
分ずから埗られたハロゲン化プノヌル溶解性の
芳銙族ポリむミドからなり、しかも、匕匵匷床
が、30〜100Kgmm2、奜たしくは35〜80Kgmm2で
あるず共に、ダング率匟性率が400〜1000
Kgmm2、奜たしくは410〜800Kgmm2皋床であり、
たた、さらに奜たしくは砎断点䌞び率が10〜70
、特に15〜60皋床である「厚さ〜200ÎŒm繋
床のフむルム状䜓シヌト状䜓」などの高物性
の芳銙族ポリむミド延䌞成圢䜓である。 この発明のように、充分な耐熱性ず共に、25
Kgmm2より高い匕匵匷床、および、350Kgmm2よ
り高いダング率匟性率を有する「ハロゲン化
プノヌルに溶解性の芳銙族ポリむミド延䌞
成圢䜓」は、埓来、党く知られおいなか぀たので
ある。 この発明の補造法においおは、䟋えば、芳銙族
テトラカルボン酞成分ず芳銙族ゞアミン成分ずの
略等モルを、有機極性溶媒䞭で、奜たしくは玄
120℃以䞊、特に奜たしくは140〜300℃の枩床重
合しお埗られた『ハロゲン化プノヌルに可溶性
である高分子量の芳銙族ポリむミド』ず、未延䌞
成圢䜓䞭の含有率が50重量以䞋、奜たしくは
〜45重量であるハロゲン化プノヌル溶媒ずか
らなる固化フむルム状䜓自己支持性フむルム、
固化繊維状䜓などの未延䌞成圢䜓を䜿甚するので
ある。 この発明では、 (1) 前蚘ハロゲン化プノヌル溶媒ず盞溶性であ
るず共に、前蚘芳銙族ポリむミドを実質的に溶
解しなく、しかも未延䌞成圢䜓に察しお膚最す
る性質を有する膚最溶媒䞭に、前述の未延䌞成
圢䜓を浞挬し、奜たしくは〜200℃特に奜
たしくは20〜150℃の枩床に、0.5〜20時間
特に〜10時間攟眮しお、未延䌞成圢䜓を
膚最溶媒で充分に膚最させた埌、 (2) 膚最した未延䌞成圢䜓をその膚最溶媒䞭で、
〜200℃特に10℃より高く、しかも、膚最
溶媒䞭の溶媒の沞点より䜎い枩床である枩床範
囲内の延䌞枩床で、1.1〜3.0倍、奜たしくは
1.2〜2.5倍に延䌞し、 (3) 最埌に、その延䌞成圢䜓から溶媒を陀去する
ず共に、延䌞成圢䜓を、奜たしくは150℃以䞊
特に奜たしくは180〜400℃の枩床で、0.5〜
10時間、特に〜時間加熱する熱凊理を行う
こずにより芳銙族ポリむミド延䌞成圢䜓を補造
するのである。 この発明においお、延䌞成圢䜓から膚最溶媒な
どを陀去するには、氎などで10〜50℃、特に20〜
45℃の枩床で抜出により行぀たり、あるいは、延
䌞成圢䜓を垞圧又は枛圧䞋加熱しお溶媒の蒞発に
より陀去するこずができ、たた、前述の延䌞成圢
䜓を150℃以䞊の高枩で加熱凊理する際には、少
なくずも前蚘延䌞成圢䜓の延䌞方向の䞡端を枠な
どで䞀定の距離に固定しお加熱凊理を行うこず
が、物性の点から奜適であるが、必ずしも、前蚘
の延䌞成圢䜓の固定が必須の芁件ではない。 たた、前蚘の加熱凊理は、最初に、玄150〜260
℃ず蚀う比范的䜎い枩床で䞀次加熱凊理し、次い
で、260〜450℃ず蚀う高い枩床で二次加熱凊理し
お行぀おもよく、その䞀次加熱においおは、枠な
どで延䌞成圢䜓の䞡端を固定しお行うこずが奜た
しい。 前蚘の芳銙族ポリむミドは、芳銙族テトラカル
ボン酞成分ず芳銙族ゞアミン成分ずから高枩での
重合で埗られたビプニルテトラカルボン酞系の
可溶性ポリむミドであるず共に、察数粘床枬定
枩床50℃、濃床0.5100ml溶媒、溶媒パ
ラクロルプノヌルが0.1〜、特に奜たしく
は0.2〜皋床であり、むミド化率〔赀倖線分析
法IR法によ぀お決定されるむミド化率であ
る〕が、90より倧きい、特に95以䞊である
ポリアミド酞に基づく赀倖吞収スペクトルのピ
ヌクが認められないポリマヌであ぀お、さら
に、ハロゲン化プノヌル溶媒に玄〜40重量
の濃床にたで均䞀に溶解できるポリマヌであるこ
ずが奜たしい。 前蚘の察数粘床は、次匏によ぀お算出された倀
である。 察数粘床自然察数溶液粘床溶媒粘床溶液の濃
床 前蚘のむミド化率を決定する赀倖線分析法で
は、詊料の赀倖線吞収スペクトルのむミド結合に
基づく吞収ピヌク1770cm-1の吞光床からむミド化
率を求めるこずができる。 前蚘のハロゲン化プノヌル溶媒は、前述のビ
プニルテトラカルボン酞系の可溶性芳銙族ポリ
むミドを50〜150℃の枩床で重量以䞊の割合
で溶解させるこずができるものであれば、どのよ
うな皮類のハロゲン化プノヌル化合物であ぀お
もよいが、特に融点が玄100℃以䞋、特に80℃以
䞋であ぀お、しかも垞圧での沞点が300℃以䞋、
特に280℃以䞋であるハロゲン化プノヌル化合
物が奜たしい。 前述ハロゲン化プノヌル溶媒ずしおは、䟋え
ば−クロルプノヌル、−クロルプノヌ
ル、−クロルプノヌル、−ブロムプノヌ
ル、−ブロムプノヌル、−ブロムプノヌ
ル、−クロル−−ヒドロキシトル゚ン、−
クロル−−ヒドロキシトル゚ン、−クロル−
−ヒドロキシトル゚ン、−クロル−−ヒド
ロキシトル゚ン、−ブロム−−ヒドロキシト
ル゚ン、−ブロム−−ヒドロキシトル゚ン、
−ブロム−−ヒドロキシトル゚ン、−ブロ
ム−−ヒドロキシトル゚ンなどを挙げるこずが
でき、あるいは、これらのハロゲン化プノヌル
化合物の皮以䞊の混合溶媒を䜿甚しおもよい。 前蚘の膚最溶媒は、前蚘の芳銙族ポリむミド
を、50℃の枩床においお、玄重量以䞊、特に
重量以䞊均䞀に溶解するこずができないこ
ず、ハロゲン化プノヌルずの盞溶性が優れおい
るこず、さらに前述の未延䌞成圢䜓に膚最する性
質を有する有機極性溶媒であればよい。そのよう
な膚最溶媒ずしおは、ハロゲン化プノヌルずア
ルコヌル類ずの混合溶媒混合溶媒ずしおは、ハ
ロゲン化プノヌルアルコヌル類の重量比が
3070〜9010、特に5050〜9010皋床である
こずが奜たしい、あるいは−ゞメチルホ
ルムアミド、−ゞ゚チルホルムアミド、
−ゞメチルアセトアミド、−ゞ゚チ
ルアセトアミド、−ゞメチルメトキシアセ
トアミドなどの−ゞ䜎玚アルキルカルボキ
シルアミド類、−ゞメチル−−むミダゟ
リゞノン、−メチル−−ピロリドン、ゞメチ
ルスルホキシド、ゞ゚チルスルホキシド、ゞメチ
ルスルホン、ゞ゚チルスルホン、ヘキサメチルス
ルホルアミドなどの有機極性溶媒を挙げるこずが
できる。 前蚘のアルコヌル類ずしおは、メタノヌル、゚
タノヌル、プロパノヌル、む゜プロパノヌル、ブ
タノヌル、アミノアルコヌルなどの炭玠数〜
皋床の䜎玚アルコヌル類を奜適に挙げるこずがで
きる。 この発明においお、前述の高分子量の芳銙族ポ
リむミドず、50重量以䞋の含有率のハロゲン化
プノヌル溶媒ずからなる固化フむルム状䜓、固
化繊維状䜓などの未延䌞成圢䜓は、(a)自己支持性
を有する、(b)ハロゲン化プノヌル溶媒を50重量
以䞋含有する、(c)延䌞倍率1.1倍より倚く延䌞
されおいない実質的に未延䌞である成圢䜓であ
り、公知の皮々の方法で補造するこずができる。
この発明では、特にその未延䌞成圢䜓の補造法が
限定されるものではなく、䟋えば、前蚘の芳銙族
ポリむミドがハロゲン化プノヌル溶媒に均䞀に
溶解しおいるポリむミド溶液を䜿甚しお、50〜
150℃で流延補膜法で補膜するか、あるいは、同
様の枩床で玡糞するこずによ぀お、圢成した液状
のフむルム状䜓たたは繊維状䜓から、同様の枩床
で溶媒の倧郚分を蒞発しお陀去する也匏法
か、たたは、氎、アルコヌルなどを䞻成分ずする
抜出溶媒で抜出法により陀去する湿匏法か、
あるいは、それらの䜵甚によ぀お陀去するかし
お、芳銙族ポリむミドず、含有率50重量以䞋の
ハロゲン化プノヌル溶媒ずからなる固化フむル
ムたたは固化繊維などの未延䌞の成圢䜓を補造す
るこずができる。 この発明では、前述のビプニルテトラカルボ
ン酞系の芳銙族ポリむミドからなる未延䌞成圢䜓
を、膚最溶媒で膚最させた埌、その膚最溶媒䞭で
延䌞し、次いで、その延䌞された成圢䜓からハロ
ゲン化プノヌルを陀去するず共に、高枩で加熱
凊理するこずに、䞻な特城があり、前述のように
延䌞の際に膚最溶媒を䜿甚するこずにより容易に
再珟性良く優れたダング率などを有する芳銙族ポ
リむミド補の延䌞成圢䜓を補造するこずができる
のである。 〔実斜䟋〕 実斜䟋および比范䟋においお、物性詊隓は、詊
料片長さ20mm、幅mmに぀いお、行぀
た。 実斜䟋 〜 3′4′−ビプニルテトラカルボン酞
二無氎物ず4′−ゞアミノゞプニル゚ヌテル
ずを、−クロルプノヌル溶媒䞭で、160℃で
時間重合およびむミド化しお埗られた芳銙族ポ
リむミド溶液〔ポリマヌ濃床18重量、ポリマ
ヌの察数粘床1.4、25℃の溶液粘床回転粘床
蚈によ぀お枬定した溶液粘床1000ポむズ〕を、
䜿甚しお、ガラス板䞊に均䞀な厚さに玄50℃で溶
液流延しお、その結果圢成された液状の薄膜を50
℃で時間也燥し、さらに50℃で24時間、真空也
燥しお、ビプニルテトラカルボン酞系の芳銙族
ポリむミドむミド化率95以䞊ず、含有率が
12重量である前蚘溶媒ずからなる厚さ50ÎŒmで
長尺である固化フむルムポリむミド−ハロゲン
化プノヌル溶媒の未延䌞フむルムを圢成し
た。 その固化フむルムを䜿甚し、75℃で、−
ゞメチル−むダ゜リゞノンを膚最溶媒ずしお䜿甚
しお、1.5時間膚最させた埌、75℃で前蚘膚最溶
媒䞭で第衚に瀺す延䌞倍率で長手方向に、延䌞
速床125分で䞀軞延䌞し、固定されたその延
䌞フむルムから50℃で氎により溶媒抜出しお膚最
溶媒を陀去し、次いで、延䌞方向の䞡端郚を枠に
固定しお、第衚に瀺す枩床および時間で凊理し
お、第衚に瀺す物性の芳銙族ポリむミド補の延
䌞フむルムを成圢した。 比范䟋および 前蚘の固化フむルム未延䌞フむルムを四蟺
を枠に固定しお、第衚に瀺す枩床および時間で
加熱凊理しお、溶媒の蒞発・陀去を行぀お、芳銙
族ポリむミドフむルムを補造した。 そのフむルムの物性を第衚に瀺す。 比范䟋および 前蚘の固化フむルム未延䌞フむルムを、膚
最溶媒䞭で膚最させたが、延䌞を党く行わずに、
四蟺を枠に固定しお、第衚に瀺す枩床および時
間で凊理しお、溶媒、膚最溶媒、および氎の蒞
発・陀去を行぀たほかは、実斜䟋ず同様にし
お、芳銙族ポリむミドフむルムを補造した。 そのフむルムの物性を第衚に瀺す。
[Industrial Application Field] The present invention relates to a novel stretched product (e.g., film, fiber, etc.) made of a specific heat-resistant aromatic polyimide and having extremely excellent physical properties, particularly a high Young's modulus, and its stretched product. This invention relates to a new method for producing molded bodies. The polyimide stretched molded product of the present invention has a high Young's modulus as well as a high level of tensile strength and heat resistance compared to this type of aromatic polyimide film molded by the usual solution casting method. In particular, they can also be used satisfactorily as thin films or fine fibers for various applications. [Prior Art] Conventionally, as a method for producing a heat-shrinkable aromatic polyimide film (stretched film),
For example, as described in Japanese Patent Publication No. 57-41330, a solution of a biphenyltetracarboxylic acid-based aromatic polyimide precursor (polyamic acid or polyamic acid) is kept at a temperature of 20 to 200°C and cast. at least 50 wt.
is converted into polyimide, and then the polyimide film is stretched in at least one direction at a stretching ratio of 100 to 500 times so that the stretching ratio is 1.05 to 5 times.
A method of stretching at a temperature of .degree. C. has been proposed. However, although it is possible to produce a heat-shrinkable polyimide film with the above method, it is difficult to forcibly stretch an "unstretched film with a high imidization rate" that has a low solvent content, or Since stretching is performed at the same time, it is difficult to perform the stretching operation stably, and
It has been difficult or virtually impossible to produce polyimide stretched films with physical properties such as high Young's modulus with good reproducibility. [Problems to be Solved by the Present Invention] The purpose of the present invention is to create a high tensile strength, etc., high Young's modulus while maintaining the excellent heat resistance originally possessed by aromatic polyimide molded products. It is an object of the present invention to provide an aromatic polyimide stretched molded article (e.g., film, fiber, etc.) with novel physical properties, and to industrially produce such a stretched aromatic polyimide molded article with high physical properties with good reproducibility. The goal is to provide a way to do so. [Requirements of the present invention] In other words, the present invention requires the use of an aromatic tetracarboxylic acid component containing 80 mol% or more of biphenyltetracarboxylic acids and an aromatic diamine component containing 70 mol% or more of diaminodiphenyl ethers. Consisting of the obtained aromatic polyimide, and
Tensile strength (ASTM D882) is 30-100Kg/ mm2 , and Young's modulus (tensile modulus; ASTM
D882) is 400 to 800 Kg/ mm2 . Further, the production method of the present invention includes a soluble aromatic polyimide obtained by polymerizing the above-mentioned aromatic tetracarboxylic acid component and aromatic diamine component in a halogenated phenol solvent, and a content of 50% by weight or less. After sufficiently swelling an unstretched molded body consisting of a halogenated phenolic solvent and a halogenated phenol solvent in a swelling solvent that is compatible with the halogenated phenolic solvent and does not substantially dissolve the aromatic polyimide, the swollen unstretched body is The molded body is placed in the swelling solvent described above,
The present invention relates to a method for producing a polyimide stretched molded body, which comprises stretching the stretched polyimide body by a factor of 1.1 to 3.0 at a stretching temperature of 0 to 200°C, and finally removing the solvent from the stretched body and heat-treating the stretched body. The aromatic tetracarboxylic acid component is, for example, 2,3,3',4'-biphenyltetracarboxylic acid or its acid dianhydride, or an ester of the acid with a lower alcohol having 1 to 5 carbon atoms; 
3',4,4'-biphenyltetracarboxylic acid or its dianhydride, or the acid having 1 to 5 carbon atoms
An aromatic tetracarboxylic acid component containing biphenyltetracarboxylic acids such as lower alcohol esters of 80 mol% or more, particularly 85 mol% or more, based on the total tetracarboxylic acid component. In this invention, in particular, as the tetracarboxylic acid component,
The aromatic tetracarboxylic acid component containing 80 mol% or more, more preferably 85 mol% or more of 3,3',4,4'-biphenyltetracarboxylic acid or its acid dianhydride is used in the aromatic polyimide obtained. It is optimal because it is excellent in solubility in halogenated phenols, moldability of the polyimide stretched molded product finally obtained, and heat resistance and mechanical properties of the stretched molded product. In addition, the above aromatic tetracarboxylic acid component is
In addition to biphenyltetracarboxylic acids, examples of tetracarboxylic acids that can be used in combination include pyromellitic acid or its acid dianhydride, benzophenonetetracarboxylic acid or its acid dianhydride, bis(3,4-dicarboxylic acid) phenyl)methane or its acid dianhydride, 2,2-bis(3,4-dicarboxyphenyl)propane or its acid dianhydride, bis(3,4-dicarboxyphenyl)sulfone or its acid dianhydride Examples include anhydrides. The aromatic diamine component mentioned above includes diaminodiphenyl ethers such as 4,4'-diaminodiphenyl ether, 3,4'-diaminodiphenyl ether, and 3,3'-diaminodiphenyl ether, and wholly aromatic diamines. The aromatic diamine component is contained in an amount of 70 mol % or more, particularly 80 mol % or more, and more preferably 90 mol % or more. In this invention, in particular, 4,4'-
An aromatic diamine component containing diaminodiphenyl ether at a content of 70 mol% or more, particularly 80 mol% or more is optimal. In addition, in the above-mentioned aromatic diamine component, in addition to diaminodiphenyl ethers, aromatic diamines that can be used in combination include, for example,
4,4'-diaminodiphenylmethane, 4,4'-diaminodiphenylpropane, 4,4'-diaminodiphenyl sulfone, 4,4'-diaminodiphenyl sulfide, o-, m- or p- Examples include phenylenediamine. In this invention, when the content of diaminodiphenyl ethers in the aromatic diamine component for producing the aromatic polyimide becomes too low, the aromatic diamine component and the aromatic tetracarboxylic acid component are separated from each other. The aromatic polyimide obtained has a reduced solubility in halogenated phenols, and it may not be possible to stably produce an unstretched molded product, so it is not suitable. However, it is not suitable because only a stretched molded product can be obtained that has poor heat resistance or any of the above-mentioned mechanical properties. In particular, the polyimide stretched molded article of the present invention contains an aromatic tetracarboxylic acid component whose main component is the above-mentioned biphenyltetracarboxylic acids (content of 90 mol or more), and a main component of diaminodiphenyl ethers (content of 80 mol or more). It is made of a halogenated phenol-soluble aromatic polyimide obtained from an aromatic diamine component (mol% or more), and has a tensile strength of 30 to 100 Kg/mm 2 , preferably 35 to 80 Kg/mm 2 In addition, Young's modulus (elastic modulus) is 400 to 1000
Kg/mm 2 , preferably about 410 to 800 Kg/mm 2 ,
More preferably, the elongation at break is 10 to 70.
%, particularly about 15 to 60%, is an aromatic polyimide stretched molded product with high physical properties such as a "film-like material (sheet-like material) with a thickness of about 5 to 200 ÎŒm". As in this invention, with sufficient heat resistance, 25
Aromatic polyimide soluble in halogenated phenols (stretched) with tensile strength higher than Kg/mm 2 and Young's modulus (modulus) higher than 350 Kg/mm 2
Conventionally, "molded bodies" were completely unknown. In the production method of the present invention, for example, approximately equimolar amounts of an aromatic tetracarboxylic acid component and an aromatic diamine component are mixed in an organic polar solvent, preferably about
A "high molecular weight aromatic polyimide that is soluble in halogenated phenols" obtained by polymerization at a temperature of 120°C or higher, particularly preferably 140 to 300°C, and a content of 50% by weight or less in the unstretched molded body, Preferably 1
~45% by weight of a halogenated phenol solvent (self-supporting film);
An unstretched molded body such as a solidified fibrous body is used. In this invention, (1) the above-mentioned compound is added to a swelling solvent that is compatible with the halogenated phenol solvent, does not substantially dissolve the aromatic polyimide, and has the property of swelling an unstretched molded article. The unstretched molded body is immersed in a swelling solvent, preferably at a temperature of 0 to 200°C (particularly preferably 20 to 150°C), for 0.5 to 20 hours (especially 1 to 10 hours). (2) The swollen unstretched molded body is soaked in the swelling solvent.
1.1 to 3.0 times, preferably at a stretching temperature of 0 to 200 °C (particularly within a temperature range higher than 10 °C and lower than the boiling point of the solvent in the swelling solvent).
(3) Finally, the solvent is removed from the stretched molded product, and the stretched molded product is stretched by 0.5 to 2.5 times, preferably at a temperature of 150°C or higher (particularly preferably 180 to 400°C).
The aromatic polyimide stretched molded article is produced by performing heat treatment for 10 hours, particularly 1 to 5 hours. In this invention, in order to remove the swelling solvent etc. from the stretched molded product, water or the like is added at 10 to 50°C, especially at 20 to 20°C.
It can be carried out by extraction at a temperature of 45°C, or it can be removed by evaporation of the solvent by heating the stretched molded body under normal pressure or reduced pressure. During the treatment, it is preferable from the viewpoint of physical properties to perform the heat treatment while fixing at least both ends of the stretched body at a certain distance with a frame, etc.; however, it is not necessary to fixation is not an essential requirement. In addition, the above heat treatment is performed at a temperature of about 150 to 260
It is also possible to carry out a primary heat treatment at a relatively low temperature of 260 to 450 °C, followed by a secondary heat treatment at a high temperature of 260 to 450 °C. It is preferable to do this in a fixed manner. The aromatic polyimide is a biphenyltetracarboxylic acid-based soluble polyimide obtained by polymerizing an aromatic tetracarboxylic acid component and an aromatic diamine component at high temperatures, and has a logarithmic viscosity (measurement temperature: 50°C, Concentration: 0.5 g/100 ml (solvent; ] is greater than 90%, especially 95% or more (no peak in the infrared absorption spectrum due to polyamic acid is observed), and furthermore, about 5 to 40% by weight of the halogenated phenolic solvent
It is preferable to use a polymer that can be uniformly dissolved up to a concentration of . The above-mentioned logarithmic viscosity is a value calculated by the following formula. Logarithmic viscosity = natural logarithm (solution viscosity/solvent viscosity)/concentration of solution In the above-mentioned infrared analysis method for determining the imidization rate, the imidization rate is determined from the absorbance of the absorption peak 1770 cm -1 based on the imide bond in the infrared absorption spectrum of the sample. can be found. The above-mentioned halogenated phenol solvent may be any type as long as it can dissolve the above-mentioned biphenyltetracarboxylic acid-based soluble aromatic polyimide at a ratio of 5% by weight or more at a temperature of 50 to 150°C. It may be a halogenated phenol compound having a melting point of about 100°C or less, especially 80°C or less, and a boiling point of 300°C or less at normal pressure,
Particularly preferred are halogenated phenol compounds whose temperature is 280°C or lower. Examples of the halogenated phenol solvents include o-chlorophenol, m-chlorophenol, p-chlorophenol, o-bromophenol, m-bromophenol, p-bromophenol, 2-chloro-4-hydroxytoluene, and 2-chlorophenol.
Chlor-5-hydroxytoluene, 3-chloro-
6-hydroxytoluene, 4-chloro-2-hydroxytoluene, 2-bromo-4-hydroxytoluene, 2-bromo-5-hydroxytoluene,
Examples include 3-bromo-6-hydroxytoluene and 4-bromo-2-hydroxytoluene, or a mixed solvent of two or more of these halogenated phenol compounds may be used. The swelling solvent is incapable of uniformly dissolving the aromatic polyimide at a temperature of 50°C at a temperature of about 3% by weight or more, especially 1% by weight or more, and has excellent compatibility with halogenated phenols. In particular, any organic polar solvent that has the property of swelling the unstretched molded article described above may be used. Such swelling solvents include mixed solvents of halogenated phenols and alcohols (as mixed solvents, the weight ratio of halogenated phenols/alcohols is
30/70 to 90/10, particularly preferably about 50/50 to 90/10), or N,N-dimethylformamide, N,N-diethylformamide,
N,N-dilower alkylcarboxylamides such as N,N-dimethylacetamide, N,N-diethylacetamide, N,N-dimethylmethoxyacetamide, 1,3-dimethyl-2-imidazolidinone, N-methyl- Examples include organic polar solvents such as 2-pyrrolidone, dimethyl sulfoxide, diethyl sulfoxide, dimethyl sulfone, diethyl sulfone, and hexamethyl sulfolamide. Examples of the alcohols include those having 1 to 6 carbon atoms, such as methanol, ethanol, propanol, isopropanol, butanol, and amino alcohol.
Preferred examples include lower alcohols of about 100%. In this invention, an unstretched molded body such as a solidified film-like body or a solidified fibrous body made of the above-mentioned high-molecular-weight aromatic polyimide and a halogenated phenol solvent with a content of 50% by weight or less is (a) self-stretched; (b) contains 50% by weight or less of a halogenated phenol solvent; (c) is a substantially unstretched molded article that has not been stretched by a stretching ratio of more than 1.1 times; It can be manufactured in
In this invention, the method for producing the unstretched molded body is not particularly limited, and for example, a polyimide solution in which the aromatic polyimide is uniformly dissolved in a halogenated phenol solvent is used to
Most of the solvent is evaporated from the liquid film or fibrous material formed by casting at 150°C or by spinning at a similar temperature. (dry method)
Or, it can be removed by an extraction method using an extraction solvent mainly composed of water, alcohol, etc. (wet method).
Alternatively, by removing them in combination, it is possible to produce an unstretched molded product such as a solidified film or solidified fiber made of aromatic polyimide and a halogenated phenol solvent with a content of 50% by weight or less. can. In this invention, an unstretched molded body made of the above-mentioned biphenyltetracarboxylic acid-based aromatic polyimide is swollen with a swelling solvent, then stretched in the swelling solvent, and then halogenated from the stretched molded body. The main characteristics are that phenols are removed and heat treatment is performed at high temperatures, and as mentioned above, by using a swelling solvent during stretching, aromatic compounds with excellent Young's modulus with good reproducibility can be easily produced. This makes it possible to produce a stretched polyimide body. [Example] In the Examples and Comparative Examples, physical property tests were conducted on sample pieces (length: 20 mm, width: 5 mm). Examples 1 to 8 Polymerization of 3,3',4,4'-biphenyltetracarboxylic dianhydride and 4,4'-diaminodiphenyl ether at 160°C for 1 hour in p-chlorophenol solvent and the aromatic polyimide solution obtained by imidization [polymer concentration: 18% by weight, polymer logarithmic viscosity: 1.4, solution viscosity at 25°C (solution viscosity measured by rotational viscometer): 1000 poise],
The resulting liquid thin film was solution cast at approximately 50 °C to a uniform thickness on a glass plate using 50 °C.
℃ for 1 hour, and then vacuum-dried at 50℃ for 24 hours to form a biphenyltetracarboxylic acid-based aromatic polyimide (imidization rate of 95% or more).
A long solidified film (unstretched film of polyimide-halogenated phenol solvent) with a thickness of 50 ÎŒm was formed, comprising 12% by weight of the above solvent. Using the solidified film, 1,3-
After swelling for 1.5 hours using dimethyl-idasolidinone as a swelling solvent, it was uniaxially stretched in the swelling solvent at 75°C at the stretching ratio shown in Table 1 in the longitudinal direction at a stretching speed of 125%/min and fixed. The stretched film was subjected to solvent extraction with water at 50°C to remove the swelling solvent, and then both ends in the stretching direction were fixed to a frame and treated at the temperature and time shown in Table 1 to obtain the first A stretched film made of aromatic polyimide having the physical properties shown in the table was molded. Comparative Examples 1 and 2 The above-mentioned solidified film (unstretched film) was fixed to a frame on all four sides and heat-treated at the temperature and time shown in Table 1 to evaporate and remove the solvent to form an aromatic polyimide film. was manufactured. The physical properties of the film are shown in Table 1. Comparative Examples 3 and 4 The solidified film (unstretched film) described above was swollen in a swelling solvent, but without any stretching.
An aromatic polyimide film was prepared in the same manner as in Example 1, except that the four sides were fixed to a frame and treated at the temperature and time shown in Table 1 to evaporate and remove the solvent, swelling solvent, and water. was manufactured. The physical properties of the film are shown in Table 1.

【衚】【table】

【衚】 延䌞倍率 枩床 時間
匕匵匷床 ダング率 䌞び率
(倍) (℃) (分)
(Kgmm2) (Kgmm2) 
[Table] Stretching ratio Temperature Time Tensile strength Young's modulus Elongation
(times) (℃) (minutes)
(Kg/mm 2 ) (Kg/mm 2 ) (%)

Claims (1)

【特蚱請求の範囲】  ビプニルテトラカルボン酞類を80モル以
䞊含有する芳銙族テトラカルボン酞成分ず、ゞア
ミノゞプニル゚ヌテル類を70モル以䞊含有す
る芳銙族ゞアミン成分ずから埗られた芳銙族ポリ
むミドからなり、しかも、匕匵匷床が30〜100
Kgmm2であるず共に、ダング率が400〜800Kgmm2
であるポリむミド延䌞成圢䜓。  ビプニルテトラカルボン酞類を80モル以
䞊含有する芳銙族テトラカルボン酞成分ず、ゞア
ミノゞプニル゚ヌテル類を70モル以䞊含有す
る芳銙族ゞアミン成分ずを、抂略等モル、ハロゲ
ン化プノヌル溶媒䞭で重合しお埗られた芳銙族
ポリむミドず、50重量以䞋の含有率のハロゲン
化プノヌル溶媒ずからなる未延䌞成圢䜓を、前
蚘ハロゲン化プノヌル溶媒ず盞溶性であるず共
に前蚘芳銙族ポリむミドを実質的に溶解しない膚
最溶媒䞭で充分に膚最させた埌、膚最した未延䌞
成圢䜓をその膚最溶媒䞭で〜200℃の延䌞枩床
で1.1〜3.0倍に延䌞し、最埌に、その延䌞成圢䜓
から溶媒を陀去するず共に延䌞成圢䜓を熱凊理す
るこずを特城ずするポリむミド延䌞成圢䜓の補造
法。
[Scope of Claims] 1. An aromatic compound obtained from an aromatic tetracarboxylic acid component containing 80 mol% or more of biphenyltetracarboxylic acids and an aromatic diamine component containing 70 mol% or more of diaminodiphenyl ethers. Made of polyimide and has a tensile strength of 30 to 100
Kg/mm 2 and Young's modulus of 400 to 800 Kg/mm 2
A polyimide stretched molded body. 2. An aromatic tetracarboxylic acid component containing 80 mol% or more of biphenyltetracarboxylic acids and an aromatic diamine component containing 70 mol% or more of diaminodiphenyl ethers in approximately equal moles in a halogenated phenol solvent. An unstretched molded body consisting of an aromatic polyimide obtained by polymerization and a halogenated phenol solvent having a content of 50% by weight or less is prepared in a manner that is compatible with the halogenated phenol solvent and substantially frees the aromatic polyimide. After sufficiently swelling in a swelling solvent that does not dissolve in 1. A method for producing a stretched polyimide molded body, which comprises removing a solvent and heat-treating the stretched molded body.
JP29477686A 1986-12-12 1986-12-12 Polyimide drawn molding and its preparation Granted JPS63147626A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29477686A JPS63147626A (en) 1986-12-12 1986-12-12 Polyimide drawn molding and its preparation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29477686A JPS63147626A (en) 1986-12-12 1986-12-12 Polyimide drawn molding and its preparation

Publications (2)

Publication Number Publication Date
JPS63147626A JPS63147626A (en) 1988-06-20
JPH0479821B2 true JPH0479821B2 (en) 1992-12-17

Family

ID=17812144

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29477686A Granted JPS63147626A (en) 1986-12-12 1986-12-12 Polyimide drawn molding and its preparation

Country Status (1)

Country Link
JP (1) JPS63147626A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03103444A (en) * 1989-09-16 1991-04-30 Mitsui Toatsu Chem Inc Production of polyimide molded article
JP4510685B2 (en) * 2004-04-26 2010-07-28 株匏䌚瀟リコヌ Endless electrophotographic image forming intermediate transfer belt, image forming apparatus having the intermediate transfer belt, and image forming method using the intermediate transfer belt
JP5381222B2 (en) * 2009-03-26 2014-01-08 宇郚興産株匏䌚瀟 Film cutting method

Also Published As

Publication number Publication date
JPS63147626A (en) 1988-06-20

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