JP2843214B2 - Polyester polymer and molded product thereof - Google Patents

Polyester polymer and molded product thereof

Info

Publication number
JP2843214B2
JP2843214B2 JP22462692A JP22462692A JP2843214B2 JP 2843214 B2 JP2843214 B2 JP 2843214B2 JP 22462692 A JP22462692 A JP 22462692A JP 22462692 A JP22462692 A JP 22462692A JP 2843214 B2 JP2843214 B2 JP 2843214B2
Authority
JP
Japan
Prior art keywords
polyester polymer
fluorene
polyester
bis
polymer according
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
JP22462692A
Other languages
Japanese (ja)
Other versions
JPH06184288A (en
Inventor
俊弘 久志本
通昭 藤
光永 五十嵐
健二 八百
種男 岡本
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.)
Kanebo Ltd
Original Assignee
Kanebo 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
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Application filed by Kanebo Ltd filed Critical Kanebo Ltd
Priority to JP22462692A priority Critical patent/JP2843214B2/en
Priority to PCT/JP1993/001070 priority patent/WO1994003521A1/en
Priority to EP93916242A priority patent/EP0653451B1/en
Priority to DE1993623551 priority patent/DE69323551T2/en
Priority to US08/374,737 priority patent/US5530086A/en
Publication of JPH06184288A publication Critical patent/JPH06184288A/en
Application granted granted Critical
Publication of JP2843214B2 publication Critical patent/JP2843214B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Polyesters Or Polycarbonates (AREA)
  • Artificial Filaments (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明はポリエステル重合体に関
し、詳しくは、透明性、耐熱性に優れ、光学的異方性が
小さく、成形性が優れているポリエステル共重合体に関
するものでとくに、9,9−ビス−(4−ヒドロキシエ
トキシフェニル)−フルオレンを含むポリエテルに関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polyester polymer, and more particularly to a polyester copolymer having excellent transparency, heat resistance, small optical anisotropy and excellent moldability. , 9-bis- (4-hydroxyethoxyphenyl) -fluorene.

【0002】[0002]

【従来の技術】近年、ポリエテルの耐熱性向上のた
め、種々の成分を共重合させたり、またポリアリレ−ト
のように全芳香族体にすることが行われてきた。9,9
−ビス−(4−ヒドロキシフェニル)−フルオレンを用
いたポリエステルについても種々の提案がなされている
が、9,9−ビス−(4−ヒドロキシエトキシフェニ
ル)−フルオレンを用いたポリエステル共重合体に関す
るものは未だみられない。
In recent years, for improving the heat resistance of the polyether scan ether, or by copolymerizing various components, also polyarylates - be the total aromatics as bets have been made. 9,9
Various proposals have been made for polyesters using -bis- (4-hydroxyphenyl) -fluorene, but those relating to polyester copolymers using 9,9-bis- (4-hydroxyethoxyphenyl) -fluorene. Is not yet seen.

【0003】即ち、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、イソフタル酸と
の重合体をその酸クロリド法から得ることが米国特許第
3、546、165号明細書に示されている。このもの
の成形性を改良するものとして、特公平4−22931
には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、イソフタル酸及び脂肪酸とを特
定の比率で混合したものを用いた耐熱性ポリエステルが
示されている。また可溶性耐熱ポリアリレ−トの製造方
法が特開昭63−152622に、また9,9−ビス−
(4−ヒドロキシフェニル)−フルオレンと、テレフタ
ル酸及びイソフタル酸との特定組成比との共重合体の特
定粘度の材料について特開昭57−192432号公報
に示されている。またこの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、イソフタ
ル酸、及び脂肪族ジカルボン酸との混合物とを用いたポ
リエステルも示されている。
That is, it is disclosed in US Pat. No. 3,546,165 that a polymer of 9,9-bis- (4-hydroxyphenyl) -fluorene and terephthalic acid and isophthalic acid can be obtained from the acid chloride method. It is shown. To improve the formability of this product, Japanese Patent Publication No. 4-22931
Discloses a heat-resistant polyester using a mixture of 9,9-bis- (4-hydroxyphenyl) -fluorene and terephthalic acid, isophthalic acid and fatty acid at a specific ratio. A method for producing a soluble heat-resistant polyarylate is disclosed in JP-A-63-152622.
JP-A-57-192432 discloses a material having a specific viscosity of a copolymer of (4-hydroxyphenyl) -fluorene and a specific composition ratio of terephthalic acid and isophthalic acid. Also disclosed is a polyester using the 9,9-bis- (4-hydroxyphenyl) -fluorene and a mixture of terephthalic acid, isophthalic acid, and aliphatic dicarboxylic acid.

【0004】しかし、これらは全て9,9−ビス−(4
−ヒドロキシフェニル)−フルオレンを用いるのであっ
て、その際の重合方法も特殊条件が必要である。即ち
9,9−ビス−(4−ヒドロキシフェニル)−フルオレ
ンの両端にはフェノ−ル性基があるために、脂肪族アル
コ−ルとは異なり、非常に反応させにくく、その為溶融
重合法ではより高温度での反応条件が必要で、得られる
ポリマ−の熱分解が生じやすくなり、着色し、品質低下
となる。また、ジカルボン酸の側の末端基を酸クロリド
にした後に、溶媒中にて脱塩酸の重合方法を用いる条件
では、均一な反応が困難で、その為分子量分布の大きい
ものが一般的に得られると言われており、また大量に必
要な触媒化合物の後処理も必要となるなど、製造方法が
複雑となり、コストアップとなる。また種々の改良にも
かかわらず、得られる材料の成形性も未だ満足とは言え
ない。また、前述の特公平4−22931号公報のポリ
エステル材料は、フェノール性の水酸基とカルボキシル
基とが直接結合しているので高温、加湿条件下では加水
分解を起こし易く、耐湿性が十分であるとはいえない。
However, these are all 9,9-bis- (4
-Hydroxyphenyl) -fluorene is used, and the polymerization method at that time also requires special conditions. That is, unlike aliphatic alcohols, 9,9-bis- (4-hydroxyphenyl) -fluorene has a phenolic group at both ends, so that it is very difficult to react. The reaction conditions at a higher temperature are required, and the resulting polymer is liable to be thermally decomposed, colored, and deteriorated in quality. In addition, under the conditions of using a polymerization method of dehydrochlorination in a solvent after the terminal group on the side of the dicarboxylic acid is converted into an acid chloride, a uniform reaction is difficult, and therefore, one having a large molecular weight distribution is generally obtained. In addition, it is necessary to carry out a large amount of post-treatment of the catalyst compound, which complicates the production method and increases the cost. Also, despite various improvements, the moldability of the resulting material is still not satisfactory. Further, the polyester material disclosed in Japanese Patent Publication No. 4-22931 is liable to be hydrolyzed under high-temperature and humidified conditions because a phenolic hydroxyl group and a carboxyl group are directly bonded, and the moisture resistance is sufficient. I can't say.

【0005】[0005]

【発明が解決しようとする課題】そこで本発明の課題
は、透明性に優れ、耐熱性があり、光学的異方性が小さ
く、成形性、寸法安定性に優れたポリエステル重合体を
提供する事にある。
An object of the present invention is to provide a polyester polymer having excellent transparency, heat resistance, small optical anisotropy, and excellent moldability and dimensional stability. It is in.

【0006】[0006]

【課題を解決するための手段】本発明者等は、上記課題
を達成すべく鋭意検討を重ねた結果、特定のポリエステ
ル重合体が、透明で、耐熱性があり、さらに光学的異方
性が小さく、成形性、寸法安定性に優れている事を見い
だし、本発明を完成するに至った。
Means for Solving the Problems The present inventors have made intensive studies to achieve the above object, and as a result, the specific polyester polymer is transparent, heat-resistant, and has a low optical anisotropy. They were found to be small and excellent in moldability and dimensional stability, and completed the present invention.

【0007】即ち、本発明は、芳香族ジカルボン酸また
はそのジエステル誘導体と一般式(1)
That is, the present invention relates to an aromatic dicarboxylic acid or a diester derivative thereof and a compound represented by the general formula (1):

【化2】 (R1 は炭素数2から4のアルキル基、R2 、R3 、R
4 、及びR5 は独立に水素または炭素数1から4のアル
キル基)で示されるジヒドロキシ化合物と炭素原子数が
2から4の脂肪族グリコールからなるポリエステル重合
体を提供するものである。
Embedded image (R 1 is an alkyl group having 2 to 4 carbon atoms, R 2 , R 3 , R
4, and R 5 are those dihydroxy compounds with number of carbon atoms represented by independently hydrogen or C 1 -C 4 alkyl) provides a reportage Riesuteru polymers such aliphatic glycols from 2 4.

【0008】以下、本発明を詳しく説明する。本発明の
ポリエステル重合体は芳香族ジカルボン酸またはそのジ
エステル誘導体と一般式(1)
Hereinafter, the present invention will be described in detail. The polyester polymer of the present invention comprises an aromatic dicarboxylic acid or a diester derivative thereof and a compound represented by the general formula (1):

【化3】 (R1 は炭素数2から4のアルキル基、R2 、R3 、R
4 、及びR5 は独立に水素または炭素数1から4のアル
キル基)で示されるジヒドロキシ化合物と炭素原子数が
2から4の脂肪族グリコールからなるポリエステル重合
体,一般式(1) で示されるジヒドロキシ化合物が、樹
脂中の全グリコール成分の10モル%以上である該ポリ
エステリエステル重合体,または極限粘度(フェノール
60重量%、1,1,2,2,−テトラクロロエタン4
0重量%の混合溶液中、20℃で測定)が0.3以上で
ある該ポリエステル重合体である。
Embedded image (R 1 is an alkyl group having 2 to 4 carbon atoms, R 2 , R 3 , R
4 and R 5 are each independently hydrogen or an alkyl group having 1 to 4 carbon atoms) and a polyester polymer comprising an aliphatic glycol having 2 to 4 carbon atoms.
The dihydroxy compound represented by the general formula (1)
The polyglycol component is at least 10 mol% of the total glycol components in the fat.
Esteriester polymer or intrinsic viscosity (phenol
60% by weight, 1,1,2,2-tetrachloroethane 4
0% by weight in a mixed solution at 20 ° C.)
One such polyester polymer.

【0009】ガラス転移温度(Tg)が90℃〜155
℃、極限粘度が0.3以上の重合度であると、その溶融
体の流動性は特に優れている。用途に応じて9,9−ビ
ス−(4−ヒドロキシエトキシフェニル)−フルオレン
の組成を変えることで、適正な成形体とすることができ
る。
A glass transition temperature (Tg) of 90 ° C. to 155
° C., the intrinsic viscosity of Ru 0.3 or more degree of polymerization der, fluidity of the melt is particularly excellent. By changing the composition of 9,9-bis- (4-hydroxyethoxyphenyl) -fluorene depending on the use, an appropriate molded article can be obtained.

【0010】前記ポリエステルの一般式(1)で表され
るジヒドロキシ化合物が10モル%より少ないと、成形
体が熱により変形しやすくなり、耐熱性が不十分であ
り、光学的異方性も大きく、成形体の安定性も低下する
ため、10モル%以上であることが好ましい。
When the amount of the dihydroxy compound represented by the general formula (1) in the polyester is less than 10 mol%, the molded article is easily deformed by heat, the heat resistance is insufficient, and the optical anisotropy is large. , Also reduces the stability of the molded body
Therefore, the content is preferably 10 mol% or more.

【0011】また、本発明のポリエスエル重合体は
ェノール60重量%、1,1,2,2,−テトラクロロ
エタン40重量%の混合溶液中、20℃で測定した極限
粘度が0.3以上であることが好ましく、更に好ましく
は0.4〜0.8である。0.3以上では、成形品の機
械的強度に優れ、0.8以下では、成形時の分子配向が
少なく、成形品の流動性が良いからである。
[0011] Poriesueru polymers of the present invention, 60% by weight phenol, 1,1,2,2, - mixed solution of 40% by weight tetrachloroethane, with an intrinsic viscosity measured at 20 ° C. of 0.3 or more preferably Rukoto Oh, and more preferably from 0.4 to 0.8. If the value is 0.3 or more,
Excellent mechanical strength, and below 0.8, the molecular orientation during molding
This is because the flow rate of the molded product is small and the flowability of the molded product is good.

【0012】本発明において、芳香族ジカルボン酸は、
テレフタル酸、イソフタル酸、ナフタレンジカルボン酸
等が挙げられるが、特にテレフタル酸が好ましい。
In the present invention, the aromatic dicarboxylic acid is
Examples thereof include terephthalic acid, isophthalic acid, and naphthalenedicarboxylic acid, and terephthalic acid is particularly preferable.

【0013】本発明において、一般式(1)で表される
ジヒドロキシ化合物は、9,9−ビス−(4−ヒドロキ
シエトキシフェニル)−フルオレン、9,9−ビス−
(4−ヒドロキシプロポキシフェニル)−フルオレン、
9,9−ビス−(4−ヒドロキシブトキシフェニル)−
フルオレン等があるが、特に9,9−ビス−(4−ヒド
ロキシエトキシフェニル)−フルオレンが好ましい。
In the present invention, the dihydroxy compound represented by the general formula (1) is 9,9-bis- (4-hydroxyethoxyphenyl) -fluorene, 9,9-bis-
(4-hydroxypropoxyphenyl) -fluorene,
9,9-bis- (4-hydroxybutoxyphenyl)-
There are fluorene and the like, and 9,9-bis- (4-hydroxyethoxyphenyl) -fluorene is particularly preferable.

【0014】9,9−ビス−(4−ヒドロキシエトキシ
フェニル)−フルオレンは、例えば、9,9−ビス−
(4−ヒドロキシフェニル)−フルオレンにエチレンオ
キサイド(以下、EO)を付加して得られる。この際、
フェノールの両水酸基にエチレンオキサイドが1分子づ
つ付加した2EO付加体(9,9−ビス−(4−ヒドロ
キシエトキシフェニル)−フルオレン)の他に、さらに
数分子過剰に付加した、3EO付加体、4EO付加体等
の不純物が含まれる事がある。3EO、4EOなどの不
純物が多くなると、ポリエステル重合体の耐熱性を低下
させる事になる。このときの2EO付加体の純度は85
%以上有れば良いが、好ましくは95%以上である。
9,9-bis- (4-hydroxyethoxyphenyl) -fluorene is, for example, 9,9-bis-
It is obtained by adding ethylene oxide (hereinafter referred to as EO) to (4-hydroxyphenyl) -fluorene. On this occasion,
In addition to the 2EO adduct (9,9-bis- (4-hydroxyethoxyphenyl) -fluorene) in which ethylene oxide is added one molecule at a time to both hydroxyl groups of phenol, a 3EO adduct, which is further added in a few molecule excess, 4EO Impurities such as adducts may be included. When impurities such as 3EO and 4EO are increased, the heat resistance of the polyester polymer is lowered. At this time, the purity of the 2EO adduct was 85.
% Or more, but preferably 95% or more.

【0015】9,9−ビス−(4−ヒドロキシプロポキ
シフェニル)−フルオレン、9,9−ビス−(4−ヒド
ロキシブトキシフェニル)−フルオレンは、例えば、
9,9−ビス−(4−ヒドロキシフェニル)−フルオレ
ンに各々、3−クロロ−プロパン−1−オール、4−ク
ロロ−プロパン−1−オールをアルカリ性条件下で反応
させれば得られる。この際の純度も、85%以上で有れ
ば良く、好ましくは95%以上である。
9,9-bis- (4-hydroxypropoxyphenyl) -fluorene and 9,9-bis- (4-hydroxybutoxyphenyl) -fluorene are, for example,
It can be obtained by reacting 9,9-bis- (4-hydroxyphenyl) -fluorene with 3-chloro-propan-1-ol and 4-chloro-propan-1-ol, respectively, under alkaline conditions. The purity at this time may be 85% or more, preferably 95% or more.

【0016】本発明において、脂肪族グリコールは、エ
チレングリコール、1,3−プロパンジオール、1、2
−プロパンジオール、1,4−ブタンジオール1,2−
ブタンジオール、1,3−ブタンジオールが挙げられる
が、中でもエチレングリコール、1,4−ブタンジオー
ルが好ましく、特にエチレングリコールが好ましい。
In the present invention, the aliphatic glycol is ethylene glycol, 1,3-propanediol,
-Propanediol, 1,4-butanediol 1,2-
Examples thereof include butanediol and 1,3-butanediol. Among them, ethylene glycol and 1,4-butanediol are preferable, and ethylene glycol is particularly preferable.

【0017】本発明のポリエステル重合体は、例えば、
エステル交換法、直接重合法等の溶融重合法、溶液重合
法、界面重合法等の公知の方法から適宜の方法を選択し
て製造できる。またその際の重合触媒等の反応条件につ
いても従来通りで良く、公知の方法を用いる事ができ
る。
The polyester polymer of the present invention is, for example,
It can be produced by selecting an appropriate method from known methods such as a melt polymerization method such as a transesterification method and a direct polymerization method, a solution polymerization method, and an interfacial polymerization method. The reaction conditions for the polymerization catalyst and the like at this time may be the same as those in the related art, and a known method can be used.

【0018】ところで本発明のポリエステル重合体を製
造する際に、溶液重合法、界面重合法等を採用する場合
には、一般に酸成分の活性種として酸クロライドを用い
たり、溶媒としてメチレンクロライド、クロロホルム等
が使用するが、ポリマ−中には副生成物である塩化物や
触媒化合物が残留し、このものは一般的に製品の品質上
良くないので、重合工程後に一般に残留異物を除去せね
ばならない。これらは、シ−ト、フィルム、プレ−ト、
繊維等の成形工程での操業性を低下させ、得られる成形
体の品質をも低下させる。例えば高温加熱時に熱分解が
多量に発生する。また光学材料等に使用する際は反射膜
や記録膜等の金属薄膜をプレ−トや基板に蒸着、スパッ
タリング等の方法で、固着するが、塩素分が大量にある
と、反射膜、記録膜を腐食し、製品の寿命や信頼性を低
下させるので、十分な、洗浄、ろ過等残留異物を除去す
る工程が必要である。
When a solution polymerization method, an interfacial polymerization method, or the like is employed for producing the polyester polymer of the present invention, an acid chloride is generally used as an active species of an acid component, or methylene chloride or chloroform is used as a solvent. Etc. are used, but chlorides and catalyst compounds as by-products remain in the polymer, which are generally inferior in terms of product quality. . These are sheets, films, plates,
It reduces the operability in the molding process of fibers and the like, and also reduces the quality of the obtained molded body. For example, a large amount of thermal decomposition occurs during high-temperature heating. When used as an optical material, a metal thin film such as a reflective film or a recording film is fixed to a plate or a substrate by a method such as evaporation or sputtering. Therefore, it is necessary to perform a sufficient process of removing residual foreign substances such as washing and filtration, since the corrosion and the life of the product are reduced.

【0019】本発明のポリエステル重合体は、溶融重合
法を用いる場合に特に良好である。即ち、9,9−ビス
−(4−ヒドロキシエトキシフェニル)−フルオレンの
化合物は、末端基が脂肪族グルコ−ルと良く似た性質で
あり、反応性が高い。これは9,9−ビス−(4−ヒド
ロキシフェニル)−フルオレンと比べると著しく異なる
ものである。この為に、酸クロリドという原料を用いる
必要もなく、従って本質的に塩素が混入しない製造方法
が可能であり、高温度での反応条件で触媒使用量を少な
くでき、残留異物が少ない方法が可能となった。
The polyester polymer of the present invention is particularly good when a melt polymerization method is used. That is, the compound of 9,9-bis- (4-hydroxyethoxyphenyl) -fluorene has a property in which the terminal group is very similar to that of the aliphatic glycol and has high reactivity. This is significantly different from 9,9-bis- (4-hydroxyphenyl) -fluorene. For this reason, it is not necessary to use a raw material called acid chloride, and therefore, a production method in which chlorine is not essentially mixed is possible, and the amount of catalyst used can be reduced under high-temperature reaction conditions, and a method of reducing residual foreign substances is possible. It became.

【0020】本発明のポリエステル重合体を溶融重合法
のエステル交換法で製造するには、一般式(1)で表さ
れるジヒドロキシ成分は樹脂中のグリコール成分の10
から95モル%であることが好ましい。これが、95モ
ル%より多い場合は、溶融重合反応が進まなかったり、
十分な重合度に達しにくいため、溶液重合法または界面
重合法で製造する。
In order to produce the polyester polymer of the present invention by a transesterification method of a melt polymerization method, the dihydroxy component represented by the general formula (1) is the same as the glycol component in the resin.
To 95 mol%. If this is more than 95 mol%, the melt polymerization reaction does not proceed,
Since it is difficult to reach a sufficient degree of polymerization, it is produced by a solution polymerization method or an interfacial polymerization method.

【0021】[0021]

【発明の効果】以上述べた如く、本発明のポリエステル
重合体は、透明性、耐熱性が良く、成形性、寸法安定
性、耐薬品性に優れた成形材料を提供でき、繊維用途、
フィルム用途、シ−ト用途等産業的に有用なものであ
る。
As described above, the polyester polymer of the present invention can provide a molding material having good transparency, heat resistance, excellent moldability, dimensional stability, and chemical resistance.
It is industrially useful for film applications, sheet applications, and the like.

【0022】[0022]

【実施例】以下実施例を挙げて本発明を具体的に説明す
る。実施例における共重合体の極限粘度、ガラス転移温
度、複屈折率、NMRは以下に示す方法で測定した。
The present invention will be specifically described below with reference to examples. The intrinsic viscosity, glass transition temperature, birefringence, and NMR of the copolymer in the examples were measured by the following methods.

【0023】(1)極限粘度 フェノール60重量%、1,1,2,2,−テトラクロ
ロエタン40重量%の混合溶液50mlに共重合体0.
15〜0.5gを80℃で溶解後、20℃で粘度を測定
し決定した。
(1) Intrinsic viscosity The copolymer 0.1 was added to 50 ml of a mixed solution of 60% by weight of phenol and 40% by weight of 1,1,2,2-tetrachloroethane.
After dissolving 15 to 0.5 g at 80 ° C, the viscosity was measured and determined at 20 ° C.

【0024】(2)ガラス転移温度 示差走査熱量計(理学電気DSC−8230)に試料約
10mgを用いて、10℃/minの昇温速度で加熱し
て測定した。JIS K 7121-1987 で定義されて
いる様にして、ガラス転移温度Tmg、補外ガラス転移
温度終了温度Tegを求めた。
(2) Glass Transition Temperature About 10 mg of a sample was measured with a differential scanning calorimeter (Rigaku Denki DSC-8230) at a heating rate of 10 ° C./min. The glass transition temperature Tmg and the extrapolated glass transition temperature end temperature Teg were determined as defined in JIS K 7121-1987 .

【0025】(3)複屈折率 カールツアイス社性偏光顕微鏡にて、セラルモン、ベレ
ック、ブレースケラー式コンペンセーターを装着し、5
46nmの単色光で測定した。測定片は樹脂を260〜
300℃で溶融、押し出し成形で、直径30mm、厚さ
1mmの円盤状の試験片を作製し、さらにその成形試験
片を160〜240℃でプレス成形し、厚み80〜15
0μのフィルムを得た。得られたフィルムを4×40m
mの短冊状に切り出し、測定試験片を得た。補外ガラス
転移終了温度 Teg+1℃の温度で測定試験片を10
%/secで40%延伸後、急冷し、延伸フィルムを得
た。これらのフィルムの複屈折率を測定した。
(3) Birefringence A Clarmont, Berek, and Brace Keller compensator were mounted on a Carl Zeiss polarizing microscope.
The measurement was performed using monochromatic light of 46 nm. Measurement piece is 260 ~
Melting at 300 ° C. and extrusion molding to produce a disc-shaped test piece having a diameter of 30 mm and a thickness of 1 mm, and press-forming the formed test piece at 160 to 240 ° C.
A 0μ film was obtained. The obtained film is 4 × 40 m
m to obtain a measurement test piece. Extrapolated glass transition end temperature 10 test specimens at a temperature of Teg + 1 ° C
After being stretched at 40% at 40% / sec, the film was rapidly cooled to obtain a stretched film. The birefringence of these films was measured.

【0026】(4)NMR バリアン社製(300MG)のFT−NMR装置を用い
て、新規ポリエステル共重合体を測定した。溶媒はトリ
フルオロ酢酸とクロロホルム混合溶媒(1:1)にて試
料を溶解し、テトラメチルシランを標品として混合し、
プロトンNMRスペクトルを測定した。
(4) NMR The novel polyester copolymer was measured using an FT-NMR apparatus manufactured by Varian (300MG). As a solvent, the sample is dissolved in a mixed solvent of trifluoroacetic acid and chloroform (1: 1), and tetramethylsilane is mixed as a standard,
The proton NMR spectrum was measured.

【0027】以下実施例中の「部」は重量部を意味す
る。 実施例1 テレフタル酸ジメチル 38部、9,9−ビス−(4−
ヒドロキシエトキシフェニル)−フルオレン 35部、
エチレングリコール 27部を原料とし、触媒として、
酢酸カルシルム 0.042部を用い、これらを反応槽
に投入し、攪拌しながら常法に従って190℃から23
0℃に徐々に加熱してエステル交換反応を行った。所定
量のメタノールを系外へ抜き出した後、重合触媒である
酸化ゲルマニウム 0.012部と、着色を防止するた
め、リン酸トリメチル 0.033部とを投入して、昇
温と減圧を徐々に行い、発生するエチレングリコールを
抜きながら、加熱槽温度を280℃、真空度を1Tor
r以下に到達させる。この条件を維持し、粘度の上昇を
待ち、2時間経過後反応を終了し、反応物を水中に押し
出してペレットを得た。
Hereinafter, "parts" in the examples means parts by weight. Example 1 38 parts of dimethyl terephthalate, 9,9-bis- (4-
(Hydroxyethoxyphenyl) -fluorene 35 parts,
Using 27 parts of ethylene glycol as a raw material, as a catalyst,
Using 0.042 parts of calcium acetate, these were charged into a reaction vessel, and stirred at 190 ° C. to 23 ° C. according to a conventional method.
The ester exchange reaction was performed by gradually heating to 0 ° C. After extracting a predetermined amount of methanol out of the system, 0.012 part of germanium oxide as a polymerization catalyst and 0.033 part of trimethyl phosphate to prevent coloring are added, and the temperature is increased and the pressure is gradually reduced. The temperature of the heating tank was set to 280 ° C and the degree of vacuum was set to 1 Torr while removing ethylene glycol generated.
r or less. While maintaining these conditions, waiting for the viscosity to rise, the reaction was terminated after 2 hours, and the reaction product was extruded into water to obtain pellets.

【0028】この共重合体の極限粘度は0.55でガラ
ス転移温度は124℃であった。樹脂を290℃で溶融
成形して、円盤上のサンプルを得た後、220℃でプレ
スし、厚さ120μのフィルムを得た。136℃で延伸
を行うと複屈折率は41×10-4であった。
This copolymer had an intrinsic viscosity of 0.55 and a glass transition temperature of 124 ° C. The resin was melt molded at 290 ° C. to obtain a sample on a disk, and then pressed at 220 ° C. to obtain a 120 μm thick film. When stretched at 136 ° C., the birefringence was 41 × 10 −4 .

【0029】実施例2 原料組成をテレフタル酸ジメチル 26部、9,9−ビ
ス−(4−ヒドロキシエトキシフェニル)−フルオレン
56部、エチレングリコール 18部とし、酢酸カル
シウムを0.028部、酸化ゲルマニウム 0.009
部、リン酸トリメチル 0.022部に変えた他は同様
に工程を進行させてして、ペレットを得た。この重合体
の極限粘度は0.43でガラス転移温度は150℃であ
った。
Example 2 The raw material composition was 26 parts of dimethyl terephthalate, 56 parts of 9,9-bis- (4-hydroxyethoxyphenyl) -fluorene and 18 parts of ethylene glycol, 0.028 parts of calcium acetate, and 0 parts of germanium oxide. .009
Parts and trimethyl phosphate were changed to 0.022 parts, and the process was carried out in the same manner to obtain pellets. The intrinsic viscosity of this polymer was 0.43 and the glass transition temperature was 150 ° C.

【0030】このポリマ−を小型射出成形機を用い、2
90℃で溶融成形して、円盤上のサンプルを得た。得ら
れたプレ−トは均一で透明であった。それを250℃で
プレスし、厚さ130μのフィルムを得た後、161℃
で延伸を行うと得られたフィルムは均一透明なものであ
った。その光学評価を行ったところ、複屈折率は12×
10-4であった。
Using a small injection molding machine, the polymer
Melt molding was performed at 90 ° C. to obtain a sample on a disk. The resulting plate was uniform and transparent. It was pressed at 250 ° C to obtain a film with a thickness of 130μ.
When the film was stretched at, the obtained film was uniformly transparent. When the optical evaluation was performed, the birefringence was 12 ×
It was 10 -4 .

【0031】実施例3〜6 原料組成比を変えた他は実施例1と同様にして測定した
結果を、表1に示す。いずれからも均一透明なものが得
られた。なお実施例5の試料のNMRスペクトルを図1
に示した。
Examples 3 to 6 Table 1 shows the results measured in the same manner as in Example 1 except that the raw material composition ratio was changed. In each case, a uniform transparent product was obtained. The NMR spectrum of the sample of Example 5 is shown in FIG.
It was shown to.

【0032】比較例1 9,9−ビス−(4−ヒドロキシエトキシフェニル)−
フルオレンを部とした他は実施1と同様にしてペレッ
トを得た結果を表1に併せて示す。表1から明かな様
に、比較例1は耐熱性が低く好ましくない。またフィル
ムを成形したところ、不均一でサンプルによりばらつき
があり良くなかった。また光学評価したところ、白濁が
生じて測定できなかった。
Comparative Example 1 9,9-bis- (4-hydroxyethoxyphenyl)-
Table 1 also shows the results of pellets obtained in the same manner as in Example 1 except that fluorene was used in an amount of 0 part. As is clear from Table 1 , Comparative Example 1 is not preferable because of low heat resistance. Further, when the film was formed, it was uneven and varied depending on the sample. In addition, when the optical evaluation was performed, it was impossible to measure due to cloudiness.

【0033】比較例2本発明の一般式(1)で示されるジヒドロキシ化合物の
代わりに 、9,9−ビス−(4−ヒドロキシフェニル)
−フルオレン35部を用いた他は実施例1と同様にして
反応を開始し、発生したメタノ−ルを除去し、エステル
交換反応を完了した後に、実施例1と同様に重合触媒を
投入し、反応を進めたが、粘度上昇が全く見られず、4
時間経過後もポリマ−の粘稠性は上がらなかった。反応
物を水中に投入したが、ペレットとならなかった。
Comparative Example 2 The dihydroxy compound of the present invention represented by the general formula (1)
Alternatively , 9,9-bis- (4-hydroxyphenyl)
-The reaction was started in the same manner as in Example 1 except that 35 parts of fluorene was used , the generated methanol was removed, and after the transesterification reaction was completed, the polymerization catalyst was charged in the same manner as in Example 1, The reaction proceeded, but no increase in viscosity was observed.
After the lapse of time, the viscosity of the polymer did not increase. The reaction was poured into water but did not form a pellet.

【0034】以上の事から、本発明のポリエステル重合
体は、重合性に富み、得られるポリエステル重合体は透
明性、耐熱性が良く、成形性に優れていることが判っ
た。
From the above, it was found that the polyester polymer of the present invention is rich in polymerizability, and the obtained polyester polymer has good transparency, heat resistance, and excellent moldability.

【0035】[0035]

【表1】 [Table 1]

【図面の簡単な説明】[Brief description of the drawings]

【図1】図1は、実施例5で得られたサンプルのNMR
スペクトル線図である。
Figure 1 is, NMR of sample obtained in Example 5
It is a spectrum diagram.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C08L 67:02 審査官 森川 聡 (56)参考文献 特開 昭63−152622(JP,A) 特開 昭57−192432(JP,A) 特開 平3−281524(JP,A) 特開 平3−73902(JP,A) 特公 平4−22931(JP,B2) (58)調査した分野(Int.Cl.6,DB名) C08G 67/12 - 63/676──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification symbol FI C08L 67:02 Examiner Satoshi Morikawa (56) References JP-A-63-152622 (JP, A) JP-A-57-192432 (JP) JP-A-3-281524 (JP, A) JP-A-3-73902 (JP, A) JP-B-4-22931 (JP, B2) (58) Fields investigated (Int. Cl. 6 , DB Name) C08G 67/12-63/676

Claims (8)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 芳香族ジカルボン酸またはそのジエステ
ル誘導体と一般式(1) 【化1】 (R 1 は炭素数2から4のアルキル基、R 2 、R 3 、R
4 、及びR 5 は独立に水素または炭素数1から4のアル
キル基)で示されるジヒドロキシ化合物と、炭素原子数
が2から4の脂肪族グリコールからなるポリエステル重
合体。
An aromatic dicarboxylic acid or a diester thereof.
Le derivative with the general formula (1) ## STR1 ## (R 1 is an alkyl group having 2 to 4 carbon atoms, R 2 , R 3 , R
4 and R 5 are independently hydrogen or an alkyl having 1 to 4 carbons.
A dihydroxy compound represented by the formula:
Is a polyester comprising an aliphatic glycol of 2 to 4
Coalescing.
【請求項2】 一般式(1)で示されるジヒドロキシ化
合物が、樹脂中の全グリコール成分の10モル%以上で
あることを特徴とする請求項1記載のポリエステル重合
体。
2. Dihydroxylation represented by the general formula (1)
The compound is at least 10 mol% of the total glycol components in the resin.
The polyester polymerization according to claim 1, wherein
body.
【請求項3】 極限粘度(フェノール60重量%、1,
1,2,2,−テトラクロロエタン40重量%の混合溶
液中、20℃で測定)が0.3以上であることを特徴と
する請求項1または2記載のポリエステル重合体。
3. Intrinsic viscosity (phenol 60% by weight, 1,
Mixed solution of 40% by weight of 1,2,2-tetrachloroethane
(Measured in liquid at 20 ° C.) is 0.3 or more
The polyester polymer according to claim 1 or 2, wherein
【請求項4】 芳香族ジカルボン酸がテレフタル酸であ
ることを特徴とする請求項1〜3のいずれかに記載のポ
リエステル重合体。
4. A polyester polymer according to any one of claims 1 to 3 in which the aromatic dicarboxylic acid is characterized in that the terephthalic acid.
【請求項5】 一般式(1)で示されるジヒドロキシ化
合物が9,9−ビス−(4−ヒドロキシエトキシフェニ
ル)−フルオレンであることを特徴とする請求項1〜4
のいずれかに記載のポリエステル重合体。
5. The method according to claim 1, wherein the dihydroxy compound represented by the general formula (1) is 9,9-bis- (4-hydroxyethoxyphenyl) -fluorene.
The polyester polymer according to any one of the above .
【請求項6】 脂肪族グリコールがエチレングリコール
であることを特徴とする請求項1〜5のいずれかに記載
のポリエステル重合体。
6. The polyester polymer according to any one of claims 1 to 5, wherein the aliphatic glycol is ethylene glycol.
【請求項7】 一般式(1)で示されるジヒドロキシ化
合物と炭素原子数2〜4の脂肪族グリコールの樹脂中の
モル比が10:90ないし95:5であること特徴と
する請求項1〜6のいずれかに記載のポリエステル重合
体。
7. to general formula (1) dihydroxy compound represented by the molar ratio of the resin of the aliphatic glycols having 2 to 4 carbon atoms is 10:90 95: claim 1, characterized in that the 5 7. The polyester polymer according to any one of items 1 to 6 .
【請求項8】 請求項1記載のポリエステル重合体から
なるポリエステル重合成形体。
8. A polyester polymer molded article comprising the polyester polymer according to claim 1 .
JP22462692A 1992-07-30 1992-07-30 Polyester polymer and molded product thereof Expired - Lifetime JP2843214B2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP22462692A JP2843214B2 (en) 1992-07-30 1992-07-30 Polyester polymer and molded product thereof
PCT/JP1993/001070 WO1994003521A1 (en) 1992-07-30 1993-07-29 Polyester polymer
EP93916242A EP0653451B1 (en) 1992-07-30 1993-07-29 Polyester
DE1993623551 DE69323551T2 (en) 1992-07-30 1993-07-29 POLYESTER
US08/374,737 US5530086A (en) 1992-07-30 1993-07-29 Polyester containing 9,9-bis(4-(2-hydroxyalkoxy)phenyl fluorene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22462692A JP2843214B2 (en) 1992-07-30 1992-07-30 Polyester polymer and molded product thereof

Publications (2)

Publication Number Publication Date
JPH06184288A JPH06184288A (en) 1994-07-05
JP2843214B2 true JP2843214B2 (en) 1999-01-06

Family

ID=16816659

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22462692A Expired - Lifetime JP2843214B2 (en) 1992-07-30 1992-07-30 Polyester polymer and molded product thereof

Country Status (1)

Country Link
JP (1) JP2843214B2 (en)

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JP2977727B2 (en) * 1994-10-11 1999-11-15 鐘紡株式会社 High molecular weight polyester resin and method for producing the same
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US7538176B2 (en) 2003-03-03 2009-05-26 Osaka Gas Co., Ltd. Polyester polymer, its moldings, and production method of the polyester polymer
JP2009167269A (en) * 2008-01-15 2009-07-30 Osaka Gas Co Ltd High-molecular weight polyester-based resin and method of producing the same
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