JPS6222829A - Production of polyamide of high degree of polymerization - Google Patents

Production of polyamide of high degree of polymerization

Info

Publication number
JPS6222829A
JPS6222829A JP16105985A JP16105985A JPS6222829A JP S6222829 A JPS6222829 A JP S6222829A JP 16105985 A JP16105985 A JP 16105985A JP 16105985 A JP16105985 A JP 16105985A JP S6222829 A JPS6222829 A JP S6222829A
Authority
JP
Japan
Prior art keywords
polyamide
organic group
group
polymerization
membered ring
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
JP16105985A
Other languages
Japanese (ja)
Inventor
Hiroo Inada
稲田 博夫
Shigeyoshi Hara
原 重義
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.)
Teijin Ltd
Original Assignee
Teijin 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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP16105985A priority Critical patent/JPS6222829A/en
Publication of JPS6222829A publication Critical patent/JPS6222829A/en
Pending legal-status Critical Current

Links

Landscapes

  • Polyamides (AREA)

Abstract

PURPOSE:To obtain a polyamide of a high degree of polymerization easily and rapidly, by increasing the MW of an amino group-terminated polyamide by reacting it with a bislactone compound. CONSTITUTION:An amino group-terminated polyamide is reacted by heating with at least either of the bislactones of formulas I and II to increase the MW of the polyamide. In the formulae, D is a tetravalent organic group which makes each of the ring structures five- or six-membered, R1 is H, or a monovalent organic group, R2 is a monovalent organic group, R3 is a bivalent organic group which makes each of the ring structures five- or six-membered, R4 is a bivalent organic group and all of said organic groups are those unreactive with the polyamide. The polyamide used is thermosetting preferably, thermoplastic having a m.p.<=350 deg.C.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は高重合度ポリアミドの製造法に関し、更に詳し
くはポリアミドの末端アミノ基と特定構造のビスラクト
ン化合物とを加熱下反応せしめて該ポリアミドの分子量
を迅速に高める、高重合度ポリアミドの製造法に関する
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method for producing a polyamide with a high degree of polymerization, and more specifically, a method for reducing the molecular weight of the polyamide by reacting the terminal amino groups of the polyamide with a bislactone compound having a specific structure under heating. This invention relates to a method for rapidly increasing polyamide with a high degree of polymerization.

従来技術 ナイロン6、ナイロン6.6.ナイロン6.10に代表
されるポリアミドは縮重合反応によって製造され、繊維
、フィルム、プラスチック等に溶融成形されて広い分野
で用いられている。近年、技術の高度化に伴い、これら
ポリアミドの機械的性質、とりわけ強力、タフネ。
Prior art nylon 6, nylon 6.6. Polyamides, typified by nylon 6.10, are manufactured by polycondensation reactions and are melt-molded into fibers, films, plastics, etc. and used in a wide range of fields. In recent years, with the advancement of technology, the mechanical properties of these polyamides have improved, especially strong and tough.

スの性能を更に高めることが望まれ、その手段として高
重合度化の研究が種々性われて℃・る。一般に、ポリア
ミドの重合度を高める手段としては高温、高真空下に溶
融状態で縮重合反応させる方法が用いられているが、こ
の方法を高重合度化に用いると長時間な裂し、かつ溶融
粘度の上昇に伴う攪拌の困難さの他に、熱分解、ゲル化
等の問題も生じる。そこで、分解等を抑える目的で、比
較的低温で1■相の縮重合反応を行う方法が考えられる
が、この方法も反応に長時間を要し、生産性が低いと〜
・う欠点がある。
It is desired to further improve the performance of polymers, and various studies have been conducted to increase the degree of polymerization as a means of achieving this goal. Generally, the method of increasing the degree of polymerization of polyamide is to carry out a polycondensation reaction in the molten state at high temperature and under high vacuum. In addition to difficulty in stirring due to increased viscosity, problems such as thermal decomposition and gelation also occur. Therefore, in order to suppress decomposition, etc., a method of performing a one-phase polycondensation reaction at a relatively low temperature is considered, but this method also requires a long time for the reaction and has low productivity.
・There are some drawbacks.

発明の目的 木兄、明の目的は、かかる欠点を解消し、ポリアミドを
短時間で高重合度化する、高重合度ポリアミドの製造法
を提供することKある。
OBJECTS OF THE INVENTION An object of Akira Kinoshita is to provide a method for producing a polyamide with a high degree of polymerization, which eliminates such drawbacks and increases the degree of polymerization of polyamide in a short period of time.

発明の構成・効果 本発明者は、従来技術の欠点を解消し、ポリアミドを短
時間で高重合度化する方法について鋭意研究の結果、特
定の構造を有するビスラクトン化合物はポリアミドの7
ミノ基末端と加熱下容易かつ迅速に反応し、#ポリアミ
ドを短時間で高重合度化し得ることを見出し、木兄間圧
到達した。
Structure/Effect of the Invention The present inventor has conducted intensive research into a method for solving the drawbacks of the prior art and increasing the degree of polymerization of polyamide in a short time, and has found that a bislactone compound having a specific structure can be
It was discovered that #polyamide could be made to a high degree of polymerization in a short time by reacting easily and quickly with the amino group terminal under heating, and the molecular pressure was reached.

すなわち、本発明は末端アミノ基を有するポリアミドと
下記式+11 、 +21で表わされるビスラクトン化
合物の少(とも1程とを加熱反応させて該ポリアミドの
分子量を高めろことを特徴とする高重合度ポリアミドの
製造法である。
That is, the present invention provides a highly polymerized polyamide characterized in that the molecular weight of the polyamide is increased by thermally reacting a polyamide having a terminal amino group with at least one bislactone compound represented by the following formula +11 or +21. This is the manufacturing method.

本発明におけるポリアミドは熱可塑性ポリアミドであり
、好ましくは350℃以下の融点を有する熱可塑性ポリ
アミドである。
The polyamide in the present invention is a thermoplastic polyamide, preferably a thermoplastic polyamide having a melting point of 350° C. or lower.

かかるポリアミドとしては、アミノ酸(またはラクタム
)自己縮合屋ポリアミド、二塩基酸・ジアミン縮合、製
ポリアミド及びこれらの共重合体が挙げら′れ、具体的
にはナイロン4、ナイロン6、ナイロン7、ナイロン9
゜ナイロン11.ナイロン12.ナイロン66゜ナイロ
ン69.ナイロン610.ナイロン612、ナイロン6
766共重合体、ナイロン6/66/6 ] 0共重合
体等の如き脂肪族ポリアミド、更にこれら脂肪族系ポリ
アミドに共重合成分として芳香族基を含有する7ミド形
成性化合物、例えばフェニレン、ナフタレン、ビフェニ
レン等の芳香族基を含有する芳香族ジアミン(例えばp
−またはm−)ユニレンジアミン+ 4+4’−または
3,4′−ジアミノジフェニルエーテル、メチレンジア
ニリン等)、芳香族ジカルボン酸(例えばテレフタル酸
、イソフタル酸、ナフタリンジカルボン酸、ジフェニル
ジカルボン酸、ジフェニルエーテルジカルボン酸等)、
芳香族アミノカル凹円、好ましくは350℃以下となる
範囲内で共重合したポリマーなどを挙げることができろ
Such polyamides include amino acid (or lactam) self-condensing polyamides, dibasic acid/diamine condensation polyamides, and copolymers thereof, and specifically, nylon 4, nylon 6, nylon 7, nylon 9
゜Nylon 11. Nylon 12. Nylon 66° Nylon 69. Nylon 610. nylon 612, nylon 6
aliphatic polyamides such as 766 copolymer, nylon 6/66/6] 0 copolymer, and 7-mide-forming compounds containing an aromatic group as a copolymer component in these aliphatic polyamides, such as phenylene and naphthalene. , aromatic diamines containing aromatic groups such as biphenylene (e.g. p
- or m-) unilene diamine + 4+4'- or 3,4'-diaminodiphenyl ether, methylene dianiline, etc.), aromatic dicarboxylic acids (e.g. terephthalic acid, isophthalic acid, naphthalene dicarboxylic acid, diphenyl dicarboxylic acid, diphenyl ether dicarboxylic acid) etc),
Examples include polymers copolymerized within the range of aromatic aminocal concave, preferably 350°C or lower.

本発明で用いるポリアミドは末端7ミノ基を有する必要
があり、該末端アミノ基の濃度はアミノ基量(−NH,
)が20油量/ 106 IIポリマー以上、更には3
0当量/ 10’ 、9ポリマ一以上、特に40当11
/10’19ポリマー以上であることが好ましい。また
ビスラクトン化合物と反応させるポリアミドの分子量は
m −クレゾール中35℃で測定した固有粘度で好まし
くは0.3以上、より好ましくは0.5以上、更に好ま
しくは0.7以上、4?に好ましくは1.0以上である
The polyamide used in the present invention must have a terminal 7-mino group, and the concentration of the terminal amino group is determined by the amount of amino groups (-NH,
) is 20 oil amount/106 II polymer or more, and even 3
0 equivalents/10', 9 polymers 1 or more, especially 40 equivalents 11
/10'19 polymer or more is preferable. The molecular weight of the polyamide to be reacted with the bislactone compound is preferably 0.3 or more, more preferably 0.5 or more, still more preferably 0.7 or more, and 4? It is preferably 1.0 or more.

本発明で用いるビスラクトン化合物は前記式111 、
 +21で表わされる化合物である。前記式fil 、
 +21中のR2は水素原子または1価の有機基であり
、該有機基としては炭素数1〜6のフルキル基、置換基
を有してもよい炭素数6〜12のアリール基、置換基を
有してもよい炭素数6〜12のジクロフルキル基等が好
ましく例示できる。特にR,としては水素原子であるこ
とが好ましい。また、鳥は1価の有機基であり、R1の
1価の有機基と同じものが好ましく、特にフェニル、ナ
フチル等の置換基な有してもよい炭素数6〜12の7リ
ール基がが5員環または6員環となる2価の有機基であ
り、炭素数2〜6のフルキレン基、置換基を有してもよ
い炭素数6〜12の7リーレン基、置換基を有してもよ
い炭素数6〜12のシクロアルキレン基等が好ましく例
示できる。
The bislactone compound used in the present invention has the above formula 111,
It is a compound represented by +21. The formula fil,
R2 in +21 is a hydrogen atom or a monovalent organic group, and the organic group includes a furkyl group having 1 to 6 carbon atoms, an aryl group having 6 to 12 carbon atoms which may have a substituent, and a aryl group having 6 to 12 carbon atoms which may have a substituent. Preferred examples include a dichlorofurkyl group having 6 to 12 carbon atoms, which may be present. In particular, R is preferably a hydrogen atom. Further, bird is a monovalent organic group, preferably the same as the monovalent organic group of R1, particularly a 7-aryl group having 6 to 12 carbon atoms which may have substituents such as phenyl and naphthyl. A divalent organic group forming a 5-membered ring or a 6-membered ring, a fullkylene group having 2 to 6 carbon atoms, a 7-rylene group having 6 to 12 carbon atoms which may have a substituent, and a 7-rylene group having 6 to 12 carbon atoms, which may have a substituent. Preferred examples include cycloalkylene groups having 6 to 12 carbon atoms.

特にR8としてはエチレン、トリメチレン、〇−フェニ
レン、1,2−シクロヘキシレン。
In particular, R8 is ethylene, trimethylene, 〇-phenylene, and 1,2-cyclohexylene.

2.3−ジシクロペンチレン等が好ましい。更にまた、
R4は2価の有機基であり、炭素数2〜12のフルキレ
ン基、置換基を廟してもよい炭素数6〜12のアリーレ
ン基、置換基を有してもよい炭素数6〜12のシクロア
ルキレン基等が好ましく例示できる。%KR,としては
フェニレン等の如きアリーレン基が好ま5員環または6
員環となる4@の有機基であり、a換基を有してもよい
炭素数6〜12の−O−、−CO−、−8−. −8O
,−、−CH,−、−CHlIC凡−9−C(CH,)
、−等である)等)が好ましく例示で(ここで2は繭記
と同じ)及び核置換基を有する上紀基が好ましい。上述
の置換基としては低級アルキル基(例えばメチル、エチ
ル等)+7リール基(例えばフェニル)が例示できる。
2,3-dicyclopentylene and the like are preferred. Furthermore,
R4 is a divalent organic group, including a fullylene group having 2 to 12 carbon atoms, an arylene group having 6 to 12 carbon atoms which may have a substituent, and a arylene group having 6 to 12 carbon atoms which may have a substituent. Preferred examples include cycloalkylene groups. %KR is preferably an arylene group such as phenylene, a 5-membered ring or a 6-membered ring.
-O-, -CO-, -8-, which is a 4@ organic group that is a membered ring and has 6 to 12 carbon atoms and may have an a substituent. -8O
,-,-CH,-,-CHlIC-9-C(CH,)
, -, etc.) are preferred examples (here, 2 is the same as Mayuki) and a kanji group having a nuclear substituent is preferred. Examples of the above-mentioned substituents include lower alkyl groups (eg, methyl, ethyl, etc.) + 7-aryl groups (eg, phenyl).

上記式to 、 +21で表わされる化合物の代表例と
しては次の如き化合物が挙げられる。
Representative examples of the compound represented by the above formula to, +21 include the following compounds.

式[11で表わされるビスラクトン化合物二0  0 
    0  HCph II      l     l     Ifo  
   0  0   0 0      0       0      phC
H但し、これら構造式でphはフェノール基を意味する
Bislactone compound represented by formula [11 200
0 HCph II l l Ifo
0 0 0 0 0 0 phC
H However, in these structural formulas, ph means a phenol group.

式(2)で表わされるビスラクトン化合物:これらビス
ラクトン化合物は1種以上を用。
Bislactone compound represented by formula (2): One or more of these bislactone compounds are used.

いることができる。I can be there.

本発明においてビスラクトン化合物の好ましい使用割合
は、ポリアミドに対し0.05〜5重量%程度、より好
ましくは0.1〜3重量%程度である。
In the present invention, the preferred proportion of the bislactone compound used is about 0.05 to 5% by weight, more preferably about 0.1 to 3% by weight, based on the polyamide.

本発明においてポリアミドとビスラクトン化合物とを反
応せしめるには両者が緊密に接触した状態で加熱する。
In the present invention, in order to cause the polyamide and the bislactone compound to react, they are heated in a state in which they are in close contact with each other.

好ましい温度は150〜350℃であり、特に好ましく
はポリアミドの溶融下で反応せしめる。反応圧力は常圧
The preferred temperature is 150 to 350°C, and the reaction is particularly preferably carried out while the polyamide is melted. The reaction pressure is normal pressure.

減圧!加圧のいずれでもよい。特に溶融下反応させる場
合に、は、ポリアミドの重合反応器中で攪拌反応させる
方法は勿論のこと、溶融成形機例えばエクストルーダー
中で両者を混合反応させることも出来る。反応時間は3
0秒〜60分、より好ましくは1分〜30分である。反
応後のポリマーの重合度(固有粘度)の増加は、初期ポ
リアミドの重合度、末端アミノ基量tビスラクトン化合
物の使用量9反応方法等によって変化するが、通常固有
粘度で0.1以上、より好ましくは0.2以上、更に好
ましくは0.3以上の増加とし、更に最終ポリマーの固
有粘度は1.5以上、更には2.0以上、%には2.5
以上とするのが好ましい。
Decompression! Either pressurization may be used. In particular, when the reaction is carried out in the melt, the reaction can be carried out with stirring in a polyamide polymerization reactor, or the two may be mixed and reacted in a melt molding machine such as an extruder. Reaction time is 3
The time period is 0 seconds to 60 minutes, more preferably 1 minute to 30 minutes. The increase in the degree of polymerization (intrinsic viscosity) of the polymer after the reaction varies depending on the degree of polymerization of the initial polyamide, the amount of terminal amino groups, the amount of bislactone compound used, 9 the reaction method, etc., but usually the intrinsic viscosity is 0.1 or more, or more. Preferably, the increase is 0.2 or more, more preferably 0.3 or more, and the intrinsic viscosity of the final polymer is 1.5 or more, more preferably 2.0 or more, and the percentage is 2.5.
It is preferable to set it as above.

本発明のポリアミドには他種の添加剤、例えば熱安定剤
、射光安定剤、艶消し剤1着色剤、増量剤、雛燃剤、制
電防止剤及び他の横側等が添加されていてもよい。
The polyamide of the present invention may also contain other additives, such as heat stabilizers, light stabilizers, matting agents, colorants, fillers, flame retardants, antistatic agents and other side effects. good.

本発明によれば、容易かつ迅速り電ポリアミドの分子量
を高めることができ、’[:浴融成形工程中でポリアミ
ドの分子量を急速に高めることができ、工業的方法とし
て有用である。
According to the present invention, the molecular weight of the polyamide can be easily and quickly increased, and the molecular weight of the polyamide can be increased rapidly during the bath melt molding process, which is useful as an industrial method.

実  施  例 以下、実施例をあげて本発明を説明する。。Example The present invention will be explained below with reference to Examples. .

なお、例中の部は重量部を意味し、また末端アミノ基〔
Mlはポリマーをm−クレゾールに溶解し、チモールブ
ルーを指示薬として0.01 Nのp−トルエンスルホ
ン酸で中和し、この中和量から求めた。
In addition, parts in the examples mean parts by weight, and terminal amino groups [
Ml was determined by dissolving the polymer in m-cresol, neutralizing it with 0.01 N p-toluenesulfonic acid using thymol blue as an indicator, and calculating the amount of neutralization.

参考例1: の合成例 無水ピロメリット酸21.9部とフェニル酢酸29.9
部及び酢酸す) 1ラム2部を攪拌機付フラスコに仕込
み、窒素気流中240〜250℃に加熱して反応によっ
て生ずる水を系外に留去した。はS:理論量の水が留去
してから反応物をジメチルホルム7ミドで再結晶し、こ
れを繰返し、融点317〜325℃の固体(BL−A)
6部、融点419〜425℃の固体(BL−B)4部を
得た。
Reference Example 1: Synthesis example of 21.9 parts of pyromellitic anhydride and 29.9 parts of phenylacetic acid
1 part and 2 parts of acetic acid were charged into a flask equipped with a stirrer and heated to 240 to 250°C in a nitrogen stream to distill water produced by the reaction out of the system. S: After the theoretical amount of water has been distilled off, the reaction product is recrystallized from dimethylformamide, and this process is repeated to obtain a solid with a melting point of 317-325°C (BL-A).
6 parts and 4 parts of a solid (BL-B) having a melting point of 419-425°C were obtained.

−考例2: ベンゾフェノン3t4t3’+4’−テトラカルボン酸
ジ無水物23.2部及びフェニル酢酸21.8部を用い
、これらを参考例1と同様に反応させ、ジメチルホルム
アミドで再結晶し、融点386〜393℃の固体(BL
−C)7部を得た。
- Example 2: Using 23.2 parts of benzophenone 3t4t3'+4'-tetracarboxylic dianhydride and 21.8 parts of phenylacetic acid, these were reacted in the same manner as in Reference Example 1, recrystallized with dimethylformamide, and the melting point 386-393℃ solid (BL
-C) 7 parts were obtained.

実施例1〜4 固有粘度1.37 、 (隅〕45当量/106.9の
ナイロン6100部を窒素ガス気流下280℃で溶融し
、これに下表に示したビスラクトン化合物の所定量を添
加し、10分間攪拌下反応させた。得られたポリマーの
固有粘度を表に示した。
Examples 1 to 4 6100 parts of nylon with an intrinsic viscosity of 1.37 and (corner) 45 equivalents/106.9 was melted at 280°C under a nitrogen gas flow, and a predetermined amount of the bislactone compound shown in the table below was added thereto. The reaction was carried out under stirring for 10 minutes.The intrinsic viscosity of the obtained polymer is shown in the table.

実施例5 固有粘度1.26 、 (NH,) 65当量/ 10
’ #のナイロン66 100部にビスラクトン化合物
BL−C1,5部を混合し、押出し機より280℃で溶
融押出した。得られたポリマーの固有粘度は2.55で
あった。尚、押出しの際のルーダ−内滞留時間は約6分
であった。
Example 5 Intrinsic viscosity 1.26, (NH,) 65 equivalents/10
1.5 parts of bislactone compound BL-C was mixed with 100 parts of ## nylon 66 and melt-extruded at 280°C from an extruder. The intrinsic viscosity of the obtained polymer was 2.55. The residence time in the router during extrusion was about 6 minutes.

Claims (1)

【特許請求の範囲】 末端アミノ基を有するポリアミドと下記式(1)、(2
)で表わされるビスラクトン化合物の少くとも1種とを
加熱反応させて該ポリアミドの分子量を高めることを特
徴とする高重合度ポリアミドの製造法。 ▲数式、化学式、表等があります▼・・・・・・・・・
・・・・・・(1) ▲数式、化学式、表等があります▼・・・・・・・・・
・・・・・・(2) 〔但し、式中のDは環構造が5員環または6員環となる
4価の有機基であり、R_1は水素原子または1価の有
機基であり、R_2は1価の有機基であり、R_3は環
構造が5員環または6員環となる2価の有機基であり、
R_4は2価の有機基であり、いずれの有機基もポリア
ミドとは非反応性の基である。〕
[Claims] A polyamide having a terminal amino group and the following formulas (1) and (2)
1. A method for producing a highly polymerized polyamide, which comprises heating and reacting at least one bislactone compound represented by the following formula to increase the molecular weight of the polyamide. ▲There are mathematical formulas, chemical formulas, tables, etc.▼・・・・・・・・・
・・・・・・(1) ▲There are mathematical formulas, chemical formulas, tables, etc.▼・・・・・・・・・
......(2) [However, D in the formula is a tetravalent organic group whose ring structure is a 5-membered ring or a 6-membered ring, R_1 is a hydrogen atom or a monovalent organic group, R_2 is a monovalent organic group, R_3 is a divalent organic group whose ring structure is a 5-membered ring or a 6-membered ring,
R_4 is a divalent organic group, and both organic groups are non-reactive with polyamide. ]
JP16105985A 1985-07-23 1985-07-23 Production of polyamide of high degree of polymerization Pending JPS6222829A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16105985A JPS6222829A (en) 1985-07-23 1985-07-23 Production of polyamide of high degree of polymerization

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16105985A JPS6222829A (en) 1985-07-23 1985-07-23 Production of polyamide of high degree of polymerization

Publications (1)

Publication Number Publication Date
JPS6222829A true JPS6222829A (en) 1987-01-31

Family

ID=15727828

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16105985A Pending JPS6222829A (en) 1985-07-23 1985-07-23 Production of polyamide of high degree of polymerization

Country Status (1)

Country Link
JP (1) JPS6222829A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5287737A (en) * 1991-07-19 1994-02-22 Toyota Jidosha Kabushiki Kaisha Device for determining misfiring of a cylinder of a multicylinder engine
JP2008508409A (en) * 2004-08-04 2008-03-21 ビーエーエスエフ ソシエタス・ヨーロピア Method for producing polymer polyamide

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5287737A (en) * 1991-07-19 1994-02-22 Toyota Jidosha Kabushiki Kaisha Device for determining misfiring of a cylinder of a multicylinder engine
JP2008508409A (en) * 2004-08-04 2008-03-21 ビーエーエスエフ ソシエタス・ヨーロピア Method for producing polymer polyamide

Similar Documents

Publication Publication Date Title
US6011125A (en) Amide modified polyesters
US4923968A (en) Melt-moldable crystalline polyimide polymer
US3832332A (en) Polyamide polymer of diamino methyl adamantane and dicarboxylic acid
US4749768A (en) Process for producing thermoplastically processable aromatic polyamide with phosphorus catalyst
EP2294113A2 (en) Process for preparing a polyamideimide, a polyamideimide and composition comprising this polyamideimide
KR0161313B1 (en) Polyimide amicester and process for preparing the same
US5532334A (en) Process for preparing polyamideimide resins having high molecular weight
US4417045A (en) Polyimides and polyimide-amides
JPH01256531A (en) Molding material
US4438256A (en) Copolyamide acid and copolyimide
US4360657A (en) Tricyclo[6.4.0.02,7 ]-dodecane-1,8,2,7-tetracarboxylic acid dianhydride and polyimides therefrom
JPS6222829A (en) Production of polyamide of high degree of polymerization
US5326830A (en) Process for preparing chain extended polymers and graft and block copolymers
Aharoni Polycondensations in the presence of aromatic phosphites: conditions and reaction products
US4391967A (en) Polyimides-polyamides from tricyclo [4.2.1.02,5 ] nonane-3,4-dimethyl-3,4,7,8-tetracarboxylic acid dianhydride and dicarboxylic acids
JPH02115227A (en) High-molecular weight (co)polyamide and preparation thereof
CN114364718A (en) Polyamide-imide polymer and method for producing same
US3468851A (en) Linear polyamide and oxazinone-containing polymer and method of producing the same
US4824932A (en) Method of manufacturing thermoplastically processible aromatic polyamides and polyamidimides from bisamide
US5569738A (en) Melt processable etherimideimide/etherimide copolymer
US3534003A (en) Polyamide imides prepared from aromatic cyclic sulfone amines and haloformylphthalic anhydrides
US4908429A (en) Special polyimides as thermoplasts
JPS6399231A (en) Soluble and heat-resistant copolyamide
US3197443A (en) Thermally stable polyamides from symmetrically substituted aromatic diamines
US4410658A (en) Polyimides-amides and copolyimides-polyamides from tetramethylcyclobutane-1,2,3,4-tetracarboxylic dianhydride, dicarboxylic acids and a mixture of diamines