JPS63152622A - Production of soluble heat-resistant polyarylate - Google Patents
Production of soluble heat-resistant polyarylateInfo
- Publication number
- JPS63152622A JPS63152622A JP20078587A JP20078587A JPS63152622A JP S63152622 A JPS63152622 A JP S63152622A JP 20078587 A JP20078587 A JP 20078587A JP 20078587 A JP20078587 A JP 20078587A JP S63152622 A JPS63152622 A JP S63152622A
- Authority
- JP
- Japan
- Prior art keywords
- polyarylate
- acid chloride
- solution
- dichloroethane
- hydroxyphenyl
- 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
Links
- 229920001230 polyarylate Polymers 0.000 title claims description 44
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 239000002904 solvent Substances 0.000 claims abstract description 19
- LXEJRKJRKIFVNY-UHFFFAOYSA-N terephthaloyl chloride Chemical class ClC(=O)C1=CC=C(C(Cl)=O)C=C1 LXEJRKJRKIFVNY-UHFFFAOYSA-N 0.000 claims abstract description 15
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 claims abstract description 13
- FDQSRULYDNDXQB-UHFFFAOYSA-N benzene-1,3-dicarbonyl chloride Chemical class ClC(=O)C1=CC=CC(C(Cl)=O)=C1 FDQSRULYDNDXQB-UHFFFAOYSA-N 0.000 claims abstract description 11
- 238000009835 boiling Methods 0.000 claims abstract description 5
- 238000001816 cooling Methods 0.000 claims abstract description 5
- YWFPGFJLYRKYJZ-UHFFFAOYSA-N 9,9-bis(4-hydroxyphenyl)fluorene Chemical compound C1=CC(O)=CC=C1C1(C=2C=CC(O)=CC=2)C2=CC=CC=C2C2=CC=CC=C21 YWFPGFJLYRKYJZ-UHFFFAOYSA-N 0.000 claims abstract description 3
- NGNBDVOYPDDBFK-UHFFFAOYSA-N 2-[2,4-di(pentan-2-yl)phenoxy]acetyl chloride Chemical class CCCC(C)C1=CC=C(OCC(Cl)=O)C(C(C)CCC)=C1 NGNBDVOYPDDBFK-UHFFFAOYSA-N 0.000 claims description 12
- 238000010528 free radical solution polymerization reaction Methods 0.000 claims description 8
- 150000002220 fluorenes Chemical class 0.000 claims description 6
- LNNIPFBETXOKIA-UHFFFAOYSA-N 4-[1-(4-hydroxyphenyl)-9h-fluoren-2-yl]phenol Chemical class C1=CC(O)=CC=C1C1=CC=C(C=2C(=CC=CC=2)C2)C2=C1C1=CC=C(O)C=C1 LNNIPFBETXOKIA-UHFFFAOYSA-N 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 20
- 238000006116 polymerization reaction Methods 0.000 abstract description 20
- 229920000642 polymer Polymers 0.000 abstract description 6
- 239000000203 mixture Substances 0.000 abstract description 2
- GUJZISPOCRVAMW-UHFFFAOYSA-N 2-[1-(2-hydroxyphenyl)-9h-fluoren-2-yl]phenol Chemical compound OC1=CC=CC=C1C1=CC=C(C=2C(=CC=CC=2)C2)C2=C1C1=CC=CC=C1O GUJZISPOCRVAMW-UHFFFAOYSA-N 0.000 abstract 1
- 230000000379 polymerizing effect Effects 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 15
- NIHNNTQXNPWCJQ-UHFFFAOYSA-N fluorene Chemical compound C1=CC=C2CC3=CC=CC=C3C2=C1 NIHNNTQXNPWCJQ-UHFFFAOYSA-N 0.000 description 12
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 10
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 8
- 230000000704 physical effect Effects 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 7
- 238000012695 Interfacial polymerization Methods 0.000 description 6
- 229920001721 polyimide Polymers 0.000 description 6
- 239000004642 Polyimide Substances 0.000 description 5
- 229920000728 polyester Polymers 0.000 description 5
- 239000003960 organic solvent Substances 0.000 description 4
- -1 that is Polymers 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 3
- 230000009477 glass transition Effects 0.000 description 3
- 230000007062 hydrolysis Effects 0.000 description 3
- 238000006460 hydrolysis reaction Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 2
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 150000001875 compounds Chemical group 0.000 description 2
- 238000000748 compression moulding Methods 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001746 injection moulding Methods 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 2
- DMCTVRQBJMBEDT-UHFFFAOYSA-N phenol;1,1,1,2-tetrachloroethane Chemical compound ClCC(Cl)(Cl)Cl.OC1=CC=CC=C1 DMCTVRQBJMBEDT-UHFFFAOYSA-N 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- ILWRPSCZWQJDMK-UHFFFAOYSA-N triethylazanium;chloride Chemical compound Cl.CCN(CC)CC ILWRPSCZWQJDMK-UHFFFAOYSA-N 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 description 1
- RXNOYRCWKRFNIM-UHFFFAOYSA-N 2-carbonochloridoylbenzoic acid Chemical compound OC(=O)C1=CC=CC=C1C(Cl)=O RXNOYRCWKRFNIM-UHFFFAOYSA-N 0.000 description 1
- LLQDKBBAVSCGKF-UHFFFAOYSA-N 2-ethyl-4-(9h-fluoren-1-yl)phenol Chemical compound C1=C(O)C(CC)=CC(C=2C=3CC4=CC=CC=C4C=3C=CC=2)=C1 LLQDKBBAVSCGKF-UHFFFAOYSA-N 0.000 description 1
- DRNOZJKDJLILAS-UHFFFAOYSA-N 4-[1-(4-hydroxyphenyl)-9h-fluoren-9-yl]phenol Chemical class C1=CC(O)=CC=C1C1C2=C(C=3C=CC(O)=CC=3)C=CC=C2C2=CC=CC=C21 DRNOZJKDJLILAS-UHFFFAOYSA-N 0.000 description 1
- SOFILIHJTWSLCM-UHFFFAOYSA-N 4-[1-(4-hydroxyphenyl)fluoren-1-yl]phenol Chemical class C1=CC(O)=CC=C1C1(C=2C=CC(O)=CC=2)C2=CC3=CC=CC=C3C2=CC=C1 SOFILIHJTWSLCM-UHFFFAOYSA-N 0.000 description 1
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 1
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 1
- 125000002252 acyl group Chemical group 0.000 description 1
- 150000001266 acyl halides Chemical class 0.000 description 1
- 150000001350 alkyl halides Chemical class 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 125000004464 hydroxyphenyl group Chemical group 0.000 description 1
- 210000000936 intestine Anatomy 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 239000003495 polar organic solvent Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 150000003512 tertiary amines Chemical class 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 238000001721 transfer moulding Methods 0.000 description 1
Landscapes
- Polyesters Or Polycarbonates (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は耐熱性、溶解性を持つポリアリレートの製造方
法を提供するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention provides a method for producing polyarylate having heat resistance and solubility.
従来の技術
芳香族ポリエステル、即ちポリアリレートは構造に基づ
く優れた性質を有するが、特に、芳香族ジカルボン酸残
基と芳香族ジヒドロキシ化合物残基及び/または芳香族
ヒドロキシカルボン酸残基から成るポリアリレートは耐
熱性に優れ、圧縮成形、トランスファー成形、射出成形
等が可能で、機械的性質、電気的性質にも優れ、機械部
品、電気、電子部品、自動車部品、食器、医療器具など
多くの分野で用いられている。BACKGROUND OF THE INVENTION Aromatic polyesters, that is, polyarylates, have excellent properties based on their structure. In particular, polyarylates consisting of aromatic dicarboxylic acid residues, aromatic dihydroxy compound residues, and/or aromatic hydroxycarboxylic acid residues It has excellent heat resistance and can be used in compression molding, transfer molding, injection molding, etc., and has excellent mechanical and electrical properties, and is used in many fields such as mechanical parts, electrical, electronic parts, automobile parts, tableware, and medical equipment. It is used.
また一般にポリエステルは製膜性がよく、室温付近では
、その機械的強度、電気物性などの物性はポリイミドと
はC同様である。しかしながら150℃以上の温度では
ポリイミドと比較して、急激にそれら物性が低下する。In general, polyester has good film-forming properties, and its physical properties such as mechanical strength and electrical properties are similar to those of polyimide C at around room temperature. However, at temperatures above 150° C., these physical properties rapidly deteriorate compared to polyimide.
このポリエステルが高温時ポリイミドと同等の機械的強
度などの物性を備えれば、無色透明性と兼ね合わせて、
用途がさらに広がることが期待される。If this polyester has physical properties such as mechanical strength equivalent to polyimide at high temperatures, it will also be colorless and transparent.
It is expected that its applications will further expand.
9.9−ビス(4−ヒドロキシフェニル)フルオレンと
テレフタル酸クロリド或いはイソフタル酸クロリドの少
なくともどちらかからポリアリレートが得られることは
米国特許第3,548,165号明細ど、英国特許1,
122,201号明細書また特開昭57−182432
号公報に開示されている。これらはいずれも界面重合法
または反応溶液を10℃に保ちながら反応を行なう低温
溶液重合法により、ポリアリレートを合成している。9. The fact that polyarylates can be obtained from 9-bis(4-hydroxyphenyl)fluorene and at least one of terephthalic acid chloride and isophthalic acid chloride is disclosed in U.S. Pat.
122,201 and JP-A-57-182432
It is disclosed in the publication No. In all of these methods, polyarylates are synthesized by an interfacial polymerization method or a low-temperature solution polymerization method in which the reaction is carried out while maintaining the reaction solution at 10°C.
本願発明者らは酸クロリド成分として、テレフタル酸ク
ロリドを用いて上記英国特許明細書、米国特許明細書ま
た特開昭57−1!32432号公報の方法に従い、重
合を行なったが、得られたポリアリレートはそれらのど
の方法においても有機溶剤に対する溶解性およびフィル
ムに成形した場合に機械強度が充分でなかった。即ち溶
解性に関しては、通常用いられる有機溶剤のなかでポリ
アリレート類に対して溶解性の高い溶剤であるクロロホ
ルムを使用しても、上記の各界面重合法で合成したポリ
アリレートは不溶部が残り溶液が白濁した。The inventors of the present application carried out polymerization using terephthalic acid chloride as the acid chloride component according to the method described in the above-mentioned British patent specification, US patent specification, and Japanese Patent Application Laid-open No. 57-1!32432. In all of these methods, polyarylate had insufficient solubility in organic solvents and insufficient mechanical strength when formed into a film. In other words, regarding solubility, even if chloroform, which is a solvent with high solubility for polyarylates among commonly used organic solvents, is used, polyarylates synthesized by each of the above interfacial polymerization methods will have an insoluble portion remaining. The solution became cloudy.
またフィルムを作製した場合、柔軟性に乏しく、非常に
脆いフィルムであった。すなわち、8.8−ビス(4−
ヒドロキシフェニル)フルオレンとテレフタル酸クロリ
ドから界面重合法によって得られるポリアリレートは可
溶性のものとは言い難いものであった。Furthermore, when a film was produced, it had poor flexibility and was very brittle. That is, 8.8-bis(4-
The polyarylate obtained from hydroxyphenyl)fluorene and terephthalic acid chloride by interfacial polymerization was hardly soluble.
以上のような欠点はポリアリレート自身の欠陥ではなく
重合方法に基づくものと考えられる。The above-mentioned defects are considered to be due to the polymerization method rather than defects in the polyarylate itself.
すなわち界面重合法は、木と有機溶剤の界面で重合が進
むが、従来原料として用いられる酸クロリド等の反応活
性な化合物を使用した場合、水による加水分解も同時に
進行する。加水分解の結果1重合末端の活性が失なわれ
、また原料のモルバランスがくずれるので、重合度が向
上しない。That is, in the interfacial polymerization method, polymerization proceeds at the interface between the wood and the organic solvent, but when a reactive compound such as acid chloride, which is conventionally used as a raw material, is used, hydrolysis by water also proceeds at the same time. As a result of hydrolysis, the activity of one polymerization terminal is lost and the molar balance of the raw materials is disrupted, so that the degree of polymerization cannot be improved.
また前述の不溶白濁部はテレフタル酸またはポリマーの
数量体、即ちオリゴマーとも考えられ、フィルムに成形
した場合これがフィルムの透明性を妨げることになると
考えられる。Further, the above-mentioned insoluble cloudy part is considered to be a mer of terephthalic acid or a polymer, that is, an oligomer, and it is thought that this will hinder the transparency of the film when it is formed into a film.
また低温溶液重合法によるポリアリレートの製造方法は
、英国特許1,122,201号、オーストリア特許3
60.7eO号に開示されているが、前者では10°C
で低温溶液重合を行ない還元粘度0.58a/gのポリ
アリレートを、後者では30℃で同様の重合を行なって
インヘレント粘度0.52di/gのポリアリレートを
得ている。これらはいずれもインヘレント粘度で0.6
di:z′gを越えるものがなく重合度がやや低いもの
であった。Furthermore, methods for producing polyarylates using low-temperature solution polymerization methods include British Patent No. 1,122,201 and Austrian Patent No. 3.
60.7eO, but in the former 10°C
In the latter case, a polyarylate with a reduced viscosity of 0.58 a/g was obtained by carrying out low-temperature solution polymerization, and a polyarylate with an inherent viscosity of 0.52 di/g was obtained by conducting a similar polymerization at 30° C. in the latter case. Both of these have an inherent viscosity of 0.6
The degree of polymerization was somewhat low as there was no polymer with di: exceeding z'g.
発明が解決しようとする問題点
本発明は、前述の界面重合法、溶液重合法の問題点を改
ηするために、重合度の向上および不溶オリゴマーを含
まない重合方法を検討して、これらの問題点を解決した
新しいポリアリレートの重合方法を開発せんとするもの
である。Problems to be Solved by the Invention The present invention aims to improve the problems of the interfacial polymerization method and solution polymerization method described above by studying methods for improving the degree of polymerization and polymerization methods that do not contain insoluble oligomers. The aim is to develop a new polyarylate polymerization method that solves these problems.
本発明は、特定の有機溶媒に完全に溶解し、自己支持性
フィルムを形成し、かつ高重合度の高耐熱性を示すポリ
アリレートの製造方法を提供するものである。The present invention provides a method for producing a polyarylate that completely dissolves in a specific organic solvent, forms a self-supporting film, and exhibits a high degree of polymerization and high heat resistance.
問題点を解決するための手段
本発明はテレフタル酸クロリド誘導体およびイソフタル
酸クロリド誘導体の少なくとも1種と9.9−ビス(4
−ヒドロキシフェニル)フルオレン類を実質的に等モル
使用し、 1.2−ジクロルエタン中で溶液重合を行な
うにあたり、予め酸クロリド誘導体を 1.2−ジクロ
ルエタンに溶解した溶液を準備し、1.2−ジクロルエ
タンに9.9−ヒス(4−ヒドロキシフェニル)フルオ
レン類を50℃以上溶媒の沸点以下の温度範囲で溶解し
、得られた9,9−ビス(4−ヒドロキシフェニル)フ
ルオレン類の溶液を冷却することなく、前記酸クロリド
誘導体の溶液中に徐々に加えて重合させ、インヘレント
粘度0 、7 du / g以上のポリアリレートとす
ることを特徴とする可溶性耐熱ポリアリレートの製造方
法である。Means for Solving the Problems The present invention provides at least one of terephthalic acid chloride derivatives and isophthalic acid chloride derivatives and 9,9-bis(4
When carrying out solution polymerization in 1,2-dichloroethane using substantially equimolar amounts of -hydroxyphenyl)fluorenes, a solution in which an acid chloride derivative was dissolved in 1,2-dichloroethane was prepared in advance, and 1.2- Dissolve 9,9-his(4-hydroxyphenyl)fluorenes in dichloroethane at a temperature range from 50°C to the boiling point of the solvent, and cool the resulting solution of 9,9-bis(4-hydroxyphenyl)fluorenes. This is a method for producing a soluble heat-resistant polyarylate, which is characterized in that the acid chloride derivative is gradually added to a solution of the acid chloride derivative and polymerized to obtain a polyarylate having an inherent viscosity of 0.7 du/g or more.
新しいポリアリレートの重合方法を開発するにあたって
本発明では具体的な目標として、溶剤可溶性、自己支持
性、#熱性の向上を目指した。In developing a new polyarylate polymerization method, the present invention specifically aimed to improve solvent solubility, self-supporting properties, and thermal properties.
溶剤可溶性に関しては、一般に溶解性の高い極性有機溶
剤またはポリエステル系の良溶剤である有機ハロゲン系
溶剤に対する+j7溶性を目指した。Regarding solvent solubility, we aimed for +j7 solubility in polar organic solvents that generally have high solubility or organic halogen solvents that are good solvents for polyester.
また目標のポリアリレートの物性としては、自己支持性
フィルムを形成する、即ち取り扱い上容易に割れたり、
粉々にならない引張り強度数kg/1m2程度を目標と
した。この為には該ポリアリレートの固有粘度(ηin
h ) 0.7a/g以上が必要である。さらに耐熱
性に関して、ガラス転移温度の目標を250〜350℃
とした。これは射出成形並びに圧縮成形が可能な最高温
度にはC等しい値であり、これに応じて熱分解温度は4
50℃以上を目指した。In addition, the target physical properties of the polyarylate are that it forms a self-supporting film, that is, it does not break easily when handled;
The target was a tensile strength of several kg/1m2 that would not shatter. For this purpose, the intrinsic viscosity (ηin
h) 0.7a/g or more is required. Furthermore, regarding heat resistance, the target glass transition temperature is 250 to 350℃.
And so. This value is equivalent to the maximum temperature at which injection molding and compression molding can be performed, and accordingly, the thermal decomposition temperature is 4 C.
We aimed for a temperature of 50℃ or higher.
本発明で原料として用いるテレフタル酸クロリド誘導体
およびイソフタル酸クロリド誘導体は、例えば酸クロリ
ド、及びベンゼン環にアルキル基などを導入した酸クロ
リド誘導体等の活性なものがあげられ、ポリエステル合
成等に広く用いられているものを使用する。The terephthalic acid chloride derivatives and isophthalic acid chloride derivatives used as raw materials in the present invention include active ones such as acid chloride and acid chloride derivatives in which an alkyl group or the like is introduced into the benzene ring, and are widely used in polyester synthesis. Use what you have.
9.9−ビス(4−ヒドロキシフェニル)フルオレン類
としては9.9−ビス(4−ヒドロキシフェニル)フル
オレン、 9.3−ビス(3−メチル−4−ヒドロキシ
フェニル)フルオレンおよび9.9−ビス(3−エチル
−4−ヒドロキシフェニル)フルオレン等を使用する。Examples of 9.9-bis(4-hydroxyphenyl)fluorenes include 9.9-bis(4-hydroxyphenyl)fluorene, 9.3-bis(3-methyl-4-hydroxyphenyl)fluorene, and 9.9-bis(4-hydroxyphenyl)fluorene. (3-ethyl-4-hydroxyphenyl)fluorene or the like is used.
反応は、テレフタル酸クロリド誘導体およびイソフタル
酸クロリド誘導体の少なくとも1種と9.8−ビス(4
−ヒドロキシフェニル)フルオレン類を実質的に等モル
使用し、生成するポリマーの溶解性、反応性を確保する
ために重合溶媒として 1.2−ジクロルエタンを用い
て行なう。The reaction involves at least one of a terephthalic acid chloride derivative and an isophthalic acid chloride derivative and 9,8-bis(4
-Hydroxyphenyl)fluorenes are used in substantially equal moles, and 1,2-dichloroethane is used as a polymerization solvent to ensure the solubility and reactivity of the resulting polymer.
すなわち、予め醜クロリド誘導体成分を 1.2−ジク
ロルエタンに溶解した溶液を準備しておき。That is, a solution in which the ugly chloride derivative component is dissolved in 1,2-dichloroethane is prepared in advance.
次いで1,2−ジクロルエタンに8,8−ビス(4−ヒ
ドロキシフェニル)フルオレン類を50℃以上溶媒の沸
点(83,5℃)以下の温度範囲で溶解し、得られた3
、9−ビス(4−ヒドロキシフェニル)フルオレン類の
溶液を冷却することなく、そのまま前記酸クロリド誘導
体の溶液中に徐々に加えて。Next, 8,8-bis(4-hydroxyphenyl)fluorenes were dissolved in 1,2-dichloroethane at a temperature range of 50°C or higher and the boiling point of the solvent (83.5°C) or lower, and the resulting 3
, the solution of 9-bis(4-hydroxyphenyl)fluorenes was gradually added as it was to the solution of the acid chloride derivative without cooling.
溶液重合法により重合させ、生成したポリアリレートが
高分子情死しすぎ、不溶化する前に、重合溶液が均一系
の状態で重合を停止させる。Polymerization is carried out by a solution polymerization method, and the polymerization is stopped while the polymerization solution is in a homogeneous state before the produced polyarylate becomes too polymeric and becomes insolubilized.
出発原料を均一に溶解させ、ポリアリレートの重合度を
上げるためには、前記のようにフルオレン類を50℃以
上溶媒の沸点以下の温度範囲で1.2−ジクロルエタン
に溶解し、得られた溶液を冷却することなくそのまま重
合反応を行なわせることが必要である。In order to uniformly dissolve the starting materials and increase the polymerization degree of polyarylate, as mentioned above, fluorenes are dissolved in 1,2-dichloroethane at a temperature range of 50°C or higher and lower than the boiling point of the solvent, and the resulting solution is It is necessary to allow the polymerization reaction to proceed as is without cooling.
重合反応を停止させた後は、副生ずる塩酸を除くために
添加しである3級アミンなどと反応して生ずる塩酸塩を
1!!過などの手段で除いてから、&!液をアセトン等
のポリアリレートの不溶性溶剤中に注ぎ入れ、生成した
ポリアリレートを析出させてポリアリレートを分離する
。After stopping the polymerization reaction, the hydrochloride produced by reacting with a tertiary amine etc. added to remove by-produced hydrochloric acid is 1! ! After removing it by means such as The liquid is poured into a polyarylate-insoluble solvent such as acetone, and the polyarylate produced is precipitated to separate the polyarylate.
さらに必要に応じて、分離したポリアリレートをクロロ
ホルム等の溶剤に溶解し、再びアセトン等に注いで再沈
、分離する精製を行ない得られたポリアリレートの純度
を高めることができる。Furthermore, if necessary, the purity of the polyarylate obtained can be increased by dissolving the separated polyarylate in a solvent such as chloroform, pouring it into acetone, etc. again, reprecipitating it, and separating it for purification.
テレフタル酸クロリド誘導体とイソフタル酸クロリド誘
導体とを混合して用いる場合には、そのモル比が1に近
づく程生成するポリアリレートの溶解性が向上するので
、必要とする物性に応じて適当に選択すればよい、いず
れの混合割合においても本発明の目的とする前述の耐熱
性、溶解性、成形性は満足される。When using a mixture of terephthalic acid chloride derivatives and isophthalic acid chloride derivatives, the solubility of the produced polyarylate improves as the molar ratio approaches 1, so they should be selected appropriately depending on the required physical properties. The above-mentioned heat resistance, solubility, and moldability, which are the objectives of the present invention, are satisfied at any mixing ratio.
また、ポリアリレートが不溶化するまでの反応時間は、
反応溶液の温度のほか、テレフタル酸クロリド誘導体と
イソフタル酸クロリド誘導体の混合割合によって変化し
、両者の比が1に近い程、ポリアリレートが不溶化しず
らくなり、不溶化するまでの反応時間は長くなる。In addition, the reaction time until polyarylate becomes insolubilized is
In addition to the temperature of the reaction solution, it changes depending on the mixing ratio of the terephthalic acid chloride derivative and the isophthalic acid chloride derivative, and the closer the ratio of both is to 1, the more difficult it is for the polyarylate to become insolubilized, and the longer the reaction time until insolubilization becomes. .
本発明の製造方法によって、得られるポリアリレートは
、その0.5gをテトラクロルエタン−フェノール(4
:8)の混合溶液100−に溶解し、30℃で測定した
固有粘度(ηimh)が少なくとも0.7dQ/g以上
、好マL < 1.OdQ/g以りとなり、該ポリア
リレートの引張強度は1 kgf/m腸2以−L、さら
に512f/ms2以上、ある場合には10kgf/m
s2以上となる。The polyarylate obtained by the production method of the present invention is prepared by mixing 0.5 g of tetrachloroethane-phenol (4
The intrinsic viscosity (ηimh) measured at 30° C. when dissolved in a mixed solution of 8) is at least 0.7 dQ/g or more, and the preferred material L < 1. OdQ/g or more, and the tensile strength of the polyarylate is 1 kgf/m2 or more, moreover 512 f/ms2 or more, and in some cases 10 kgf/m
s2 or more.
未発IIでは、溶媒として1.2−ジクロルエタンを用
い、溶液重合法で反応を行なうので、水が共存せず、界
面重合法に比べ、フタル酸クロリドの加水分解による失
活などが防止できる。In undeveloped II, 1,2-dichloroethane is used as a solvent and the reaction is carried out by a solution polymerization method, so water does not coexist and deactivation of phthalic acid chloride due to hydrolysis can be prevented compared to an interfacial polymerization method.
得られるポリアリレートは高熱時酸化により着色する場
合がある。これはポリマー末端のフェノール基、または
酸クロリド基が、精製などに用いられるアセトン中の木
により加水分解し、カルボキシル基となっているが、こ
の内、フェノール基は特に酸化され易く、着色の原因と
なる0着色を避けたい場合は末端をアルキル基、または
アシル基により保護すればよい。The resulting polyarylate may become colored due to oxidation at high temperatures. This is because the phenol group or acid chloride group at the end of the polymer is hydrolyzed by wood in the acetone used for purification and becomes a carboxyl group, but the phenol group is particularly easy to oxidize and is the cause of discoloration. If you want to avoid coloring, the terminal may be protected with an alkyl group or an acyl group.
具体的には、アルキルハライド、またはアシルハライド
、特にアセチルハライド、またはベンゾイルハライドを
作用させるとよい。Specifically, it is preferable to use an alkyl halide or an acyl halide, particularly an acetyl halide or a benzoyl halide.
以下実施例に基づき、詳細に説明する。The following will be described in detail based on examples.
実施例
実施例1
8.3−ビス(4−ヒドロキシフェニル)フルオレン3
.5gを 1.2−ジクロルエタン70dに加え。Examples Example 1 8.3-bis(4-hydroxyphenyl)fluorene 3
.. Add 5g to 70d of 1,2-dichloroethane.
60℃に加熱して溶解した。この溶液にトリエチルアミ
ン2.2gを加えた溶液を冷却することなく、予め準備
したテレフタル酸クロリド1.81gとインフタル酸ク
ロリド0.2gのジクロルエタン30鍛溶液に5分間か
けて滴下した。その後、室温で攪拌を続けると、トリエ
チルアミン塩酸塩の析出とともに粘度が上昇した。3〜
5時間攪拌後、トリエチルアミン塩酸塩を濾過した溶液
をアセトン中に注いだ。It was heated to 60°C to dissolve it. A solution obtained by adding 2.2 g of triethylamine to this solution was added dropwise over 5 minutes to a dichloroethane 30 solution containing 1.81 g of terephthalic acid chloride and 0.2 g of inphthalic acid chloride prepared in advance without cooling. Thereafter, when stirring was continued at room temperature, triethylamine hydrochloride was precipitated and the viscosity increased. 3~
After stirring for 5 hours, the filtered solution of triethylamine hydrochloride was poured into acetone.
析出したポリアリレートを濾過、クロロホルムに溶解し
、再びアセトンに注いだ、再沈をさらに2度行なって精
製した。得られたポリアリレートはガラス転移温度30
5℃、分解温度505℃であった。ポリアリレート0.
5gをテトラクロルエタン−フェノール(4:8)の混
合溶液100−に溶解し、30℃において測定した固有
粘度(ηinh )は1.31a/gであった。The precipitated polyarylate was filtered, dissolved in chloroform, poured into acetone again, and reprecipitated twice for purification. The obtained polyarylate has a glass transition temperature of 30
The decomposition temperature was 505°C. Polyarylate 0.
5 g was dissolved in a mixed solution of tetrachloroethane-phenol (4:8) 100° C., and the intrinsic viscosity (ηinh) measured at 30° C. was 1.31 a/g.
得られたポリアリレートをN−メチルピロリドンに溶解
した後、ガラス板上に硫延して、無色透明のフィルムを
得た。フィルムの引張強度は19.8kg/腸lI2で
あった。The obtained polyarylate was dissolved in N-methylpyrrolidone and then sulfur-rolled onto a glass plate to obtain a colorless and transparent film. The tensile strength of the film was 19.8 kg/intestine II2.
また得られたポリアリレートは、クロロホルム、 1.
2−ジクロルエタン、 1,1,2.2−テトラクロ
ルエタンなどのハロゲン系溶剤、ディメチルホルムアミ
ド、ディメチルアセトアミド、ディメチルスルホキシド
、テトラヒドロフランの溶剤に完全に溶解した。In addition, the obtained polyarylate contains chloroform, 1.
It was completely dissolved in halogenated solvents such as 2-dichloroethane and 1,1,2.2-tetrachloroethane, and in solvents such as dimethylformamide, dimethylacetamide, dimethylsulfoxide, and tetrahydrofuran.
実施例2〜5
実施例1に用いたテレフタル酸クロリドとイソフタル酸
クロリドを第1表のように変えて、その他は全く同様に
反応を行なった。得られたポリアリレートも物性も第1
表に示した。また溶剤可溶性も実施例1の場合と同様で
あった。Examples 2 to 5 The reaction was carried out in exactly the same manner as in Example 1 except that the terephthalic acid chloride and isophthalic acid chloride used were changed as shown in Table 1. The obtained polyarylate also has first-class physical properties.
Shown in the table. Further, the solvent solubility was also the same as in Example 1.
第1表
実施例6
実施例1において、テレフタル酸クロリドとイソフタル
酸クロリドを用いることにかえ、テレフタル酸クロリド
のみ2.1g用いた。また反応時間を2時間以内とした
。その他は同様に反応を行なった。得られたポリアリレ
ートのガラス転移温度308℃S熱分解温度505℃、
また固有粘度(ηinh )は1.39 du/gであ
った。またフィルム形成後の引張強度は15.8kgf
/am2であった。溶剤可溶性は実施例1の場合と同様
であった。Table 1 Example 6 In Example 1, instead of using terephthalic acid chloride and isophthalic acid chloride, 2.1 g of only terephthalic acid chloride was used. Further, the reaction time was set to within 2 hours. The other reactions were carried out in the same manner. The glass transition temperature of the obtained polyarylate was 308°C, the thermal decomposition temperature was 505°C,
Further, the intrinsic viscosity (ηinh) was 1.39 du/g. In addition, the tensile strength after film formation is 15.8 kgf.
/am2. Solvent solubility was the same as in Example 1.
発明の効果
本発明は高耐熱性でかつ可溶性を備え、さらに高強度の
フィルム形性能をもつ新規なポリアリレートの製法を提
供するもので、該ポリアリレートはポリイミドと同様熱
特性にも優れており、また、透明性さらに無色のフィル
ムを提供しうるので、産業界、特に電気、電子部門に巾
広く用いられる。Effects of the Invention The present invention provides a method for producing a new polyarylate that is highly heat resistant and soluble, and also has high strength film-forming performance.The polyarylate has excellent thermal properties similar to polyimide. Moreover, since it can provide a transparent and colorless film, it is widely used in industry, especially in the electrical and electronic sectors.
さらに本発明のポリアリレートは唯一高温物性の優れた
ポリイミドフィルムと同等の物性を示すばかりでなく、
易加工性のため有機/\ロゲン系溶剤に対する可溶性の
付与により、ポリイミドの欠点である加工面の幾つかの
欠点を改善したものである。Furthermore, the polyarylate of the present invention not only exhibits physical properties equivalent to the only polyimide film with excellent high-temperature physical properties, but also
It improves some of the disadvantages of polyimide in terms of processing by imparting solubility in organic/\logenic solvents for ease of processability.
Claims (1)
ド誘導体の少なくとも1種と9,9−ビス(4−ヒドロ
キシフェニル)フルオレン類を実質的に等モル使用し、
1,2−ジクロルエタン中で溶液重合を行なうにあたり
、予め酸クロリド誘導体を1,2−ジクロルエタンに溶
解した溶液を準備し、1,2−ジクロルエタンに9,9
−ビス(4−ヒドロキシフェニル)フルオレン類を50
℃以上溶媒の沸点以下の温度範囲で溶解し、得られた9
,9−ビス(4−ヒドロキシフェニル)フルオレン類の
溶液を冷却することなく、前記酸クロリド誘導体の溶液
中に徐々に加えて重合させ、インヘレント粘度0.7d
l/g以上のポリアリレートとすることを特徴とする可
溶性耐熱ポリアリレートの製造方法。using substantially equimolar amounts of at least one of a terephthalic acid chloride derivative and an isophthalic acid chloride derivative and 9,9-bis(4-hydroxyphenyl)fluorenes,
When performing solution polymerization in 1,2-dichloroethane, a solution of an acid chloride derivative dissolved in 1,2-dichloroethane is prepared in advance, and 9,9-dichloroethane is dissolved in 1,2-dichloroethane.
-50 bis(4-hydroxyphenyl)fluorenes
9 obtained by dissolving in a temperature range of ℃ or higher and lower than the boiling point of the solvent.
, 9-bis(4-hydroxyphenyl)fluorenes was gradually added to the solution of the acid chloride derivative without cooling and polymerized to give an inherent viscosity of 0.7 d.
A method for producing a soluble heat-resistant polyarylate, characterized in that the polyarylate is 1/g or more.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19045186 | 1986-08-15 | ||
JP61-190451 | 1986-08-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63152622A true JPS63152622A (en) | 1988-06-25 |
Family
ID=16258348
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20078587A Pending JPS63152622A (en) | 1986-08-15 | 1987-08-13 | Production of soluble heat-resistant polyarylate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63152622A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5115372A (en) * | 1989-05-05 | 1992-05-19 | Minnesota Mining And Manufacturing Company | High purity aromatic polyesters |
US5248838A (en) * | 1990-10-30 | 1993-09-28 | Minnesota Mining And Manufacturing Company | Process for preparing bisphenol fluorene compounds |
US5295040A (en) * | 1989-05-05 | 1994-03-15 | Minnesota Mining And Manufacturing Company | High purity aromatic polyesters |
US5318938A (en) * | 1989-05-05 | 1994-06-07 | Minnesota Mining And Manufacturing Company | Thermographic elements |
US5530086A (en) * | 1992-07-30 | 1996-06-25 | Kanebo, Ltd. | Polyester containing 9,9-bis(4-(2-hydroxyalkoxy)phenyl fluorene |
-
1987
- 1987-08-13 JP JP20078587A patent/JPS63152622A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5115372A (en) * | 1989-05-05 | 1992-05-19 | Minnesota Mining And Manufacturing Company | High purity aromatic polyesters |
US5295040A (en) * | 1989-05-05 | 1994-03-15 | Minnesota Mining And Manufacturing Company | High purity aromatic polyesters |
US5318938A (en) * | 1989-05-05 | 1994-06-07 | Minnesota Mining And Manufacturing Company | Thermographic elements |
US5248838A (en) * | 1990-10-30 | 1993-09-28 | Minnesota Mining And Manufacturing Company | Process for preparing bisphenol fluorene compounds |
US5530086A (en) * | 1992-07-30 | 1996-06-25 | Kanebo, Ltd. | Polyester containing 9,9-bis(4-(2-hydroxyalkoxy)phenyl fluorene |
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