JPS6067530A - Copolyester - Google Patents

Copolyester

Info

Publication number
JPS6067530A
JPS6067530A JP17639283A JP17639283A JPS6067530A JP S6067530 A JPS6067530 A JP S6067530A JP 17639283 A JP17639283 A JP 17639283A JP 17639283 A JP17639283 A JP 17639283A JP S6067530 A JPS6067530 A JP S6067530A
Authority
JP
Japan
Prior art keywords
ethane
acid
mol
chlorophenoxy
formula
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
JP17639283A
Other languages
Japanese (ja)
Inventor
Shunei Inoue
井上 俊英
Masaru Okamoto
勝 岡本
Koichi Abe
晃一 阿部
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP17639283A priority Critical patent/JPS6067530A/en
Publication of JPS6067530A publication Critical patent/JPS6067530A/en
Pending legal-status Critical Current

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  • Polyesters Or Polycarbonates (AREA)

Abstract

PURPOSE:To provide a polyester capable of giving, in good formability, formed article of high strength and high modulus with adequately high melting point, having both specific two sorts of carboxylate units. CONSTITUTION:The objective copolyester having (A) 50-98mol% of a carboxylate unit of formula I and (B) 50-2mol% of a second carboxylate unit of formula II (R is of formula III or IV). The manufacturing process is as follows: (1) 50-98mol%, on a recurring unit basis, of polyethylene-1,2-bis(2-chlorophenoxy) ethane-4,4'-dicarboxylate with an intrinsic viscosity 0.4-1.20 and (2) 50-2mol% of an acyloxy aromatic carboxylic acid are made to react, at 250-300 deg.C, to prepare a prepolymer while eliminating the oxy acid generated. The resulting prepolymer is heated to 290-310 deg.C under a reduced pressure <=1mm.Hg to further proceed with a polycondensation.

Description

【発明の詳細な説明】 本発明は成形性がすぐれ、高弾性率の成形品を与え得る
新規な共重合ポリエステルに関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a novel copolyester that has excellent moldability and can provide molded articles with a high modulus of elasticity.

ポリエチレン−1,2−ビス(2−クロルフェノキシ)
エタン−4,4′−ジカルボキシレートは高弾性率m維
を与えることが知られているが(特公昭49−1795
号公報)、溶融粘度が高く紡糸性の不良なこと、屈曲強
度の低いという欠点を有する。また、このポリマからの
フィルムも高弾性率になるが、延伸時の延伸張力が大き
く延伸性が必ずしも十分ではないこと、フィルムの耐衝
撃性の不良なことがわかった。
Polyethylene-1,2-bis(2-chlorophenoxy)
Ethane-4,4'-dicarboxylate is known to provide m-fibers with high elastic modulus (Japanese Patent Publication No. 49-1795
(Japanese Patent Publication No. 2003-110023), it has the drawbacks of high melt viscosity, poor spinnability, and low flexural strength. Furthermore, although a film made from this polymer also has a high modulus of elasticity, it was found that the stretching tension during stretching was large and the stretchability was not necessarily sufficient, and the film had poor impact resistance.

そこで本発明者らは、上記ポリエステルの欠点を改良し
、融点がそれ程高くなく、かつ高強度で高弾性率の成形
品を与え得る共重合ポリエステルの取得を目的として検
討した結果、上記目的に合致した新規な共重合ポリエス
テルを見出し、本発明をなすに到った。
Therefore, the present inventors investigated with the aim of improving the drawbacks of the above polyester and obtaining a copolyester that does not have a very high melting point and can provide molded products with high strength and high modulus of elasticity. We have discovered a new copolymerized polyester, and have completed the present invention.

すなわち本発明は、50モル%を越え98モル%以下・
の次式(I)で示されるカルボキシレート単位 しl および50モル%未満2モル%以上の次式(IF)で示
されるカルボキシレート単位 ? (−ORC+(Il を示す)を有する共重合ポリエステルを提供するもので
ある。
That is, the present invention provides for
Is the carboxylate unit represented by the following formula (I) l and less than 50 mol % or more than 2 mol % of the carboxylate unit represented by the following formula (IF)? (-ORC+ (indicating Il)) is provided.

出発原料として用いるポリエチレン−1,2−ビス(2
−クロルフェノキシ)エタン−4,4′−ジカルボキシ
レートは下記構造単位しl で示されるポリエステルである1゜固有粘度0.4〜1
.20のものが好ましく用いられる。
Polyethylene-1,2-bis(2
-Chlorphenoxy)ethane-4,4'-dicarboxylate is a polyester having the structural unit shown below and having an intrinsic viscosity of 1° and 0.4 to 1.
.. 20 is preferably used.

なお、このポリエチレン−1,2−ビス(2−クロルフ
ェノキシ)エタン−4,4’−ジカルボキシレート重合
体は、1,2−ビス(2−クロルフェノキシ)エタン−
4,4’−ジカルボン酸またはそのエステル形成性誘導
体とエチレングリコールとを重縮合することにより得ら
れるが、さらに1−(2−クロルフェノキシ)−2(フ
ェノキシ)エタン−4,4′−ジカルボン酸、1.2−
ビス(フェノキシ)エタン−4,4′−ジカルボン酸、
2.6−ナフタレンジカルボン酸、4.4′−ジフェニ
ルジカルボン酸、3.3’−ジフェニルジカルボン酸、
3.4’−ジフェニルカルボン酸、2.2’−ジフェニ
ルジカルボン酸、テレフタル酸、ヘキサヒドロテレフタ
ル酸などの芳香族および脂環式ジカルボン酸またはこれ
らのエステル形成性誘導体およびジエチレングリコール
、 1.3−プロパンジオール、1,4−ブタンジオー
ル、1,6−ヘキサンジオールなどのグリコール成分を
少量共重合成分として含有することができる。最も好ま
しい共重合成分は1−(2−クロルフェノキシ)−2(
フェノキシ)エタン−4、4’ −= 3− ジカルボン酸成分である。
Note that this polyethylene-1,2-bis(2-chlorophenoxy)ethane-4,4'-dicarboxylate polymer is 1,2-bis(2-chlorophenoxy)ethane-4,4'-dicarboxylate polymer.
It is obtained by polycondensing 4,4'-dicarboxylic acid or its ester-forming derivative with ethylene glycol, and further contains 1-(2-chlorophenoxy)-2(phenoxy)ethane-4,4'-dicarboxylic acid. , 1.2-
bis(phenoxy)ethane-4,4'-dicarboxylic acid,
2.6-naphthalenedicarboxylic acid, 4.4'-diphenyldicarboxylic acid, 3.3'-diphenyldicarboxylic acid,
3. Aromatic and alicyclic dicarboxylic acids such as 4'-diphenylcarboxylic acid, 2.2'-diphenyldicarboxylic acid, terephthalic acid, hexahydroterephthalic acid, or ester-forming derivatives thereof, diethylene glycol, 1.3-propane A small amount of glycol components such as diol, 1,4-butanediol, and 1,6-hexanediol can be contained as a copolymer component. The most preferred copolymerization component is 1-(2-chlorophenoxy)-2(
phenoxy)ethane-4,4'-=3-dicarboxylic acid component.

このポリエチレン−1,2−ビス(2−クロルフェノキ
シ)エタン−4,4’−ジカルボキシレートをくり返し
単位に換算して50〜98モル%とくに55〜95モA
/%にアシルオキシ芳香族カルボン酸50〜2モル%、
とくに45〜5モル%をさらに反応させ、重縮合するこ
とにより本発明の共重合ポリエステルが製造できる。こ
こでいうアシルオキシ芳香族カルボン酸としてはP−ア
シルオキシ安息香酸および/または6−アシルオキシ−
2−ナフトエ酸であり例えばP−アセトキシ安息香酸、
6−アセトキシ−2−ナフトエ酸などである。これらア
シルオキシ芳香族カルボン酸の使用量が全体の50モル
%以上になると異方性(液晶)を示し、異方性の大きい
フィルム、樹脂になり好ましくない。また2モル%未満
では、本発明の目的である紡糸性、繊維の屈曲強度、フ
ィルム延伸性、耐衝撃性の改良効果が小さく本発明の目
的を達成すること 4− ができない。
This polyethylene-1,2-bis(2-chlorophenoxy)ethane-4,4'-dicarboxylate is 50 to 98 mol%, especially 55 to 95 mol% in terms of repeat units.
/% acyloxy aromatic carboxylic acid 50-2 mol%,
In particular, the copolymerized polyester of the present invention can be produced by further reacting and polycondensing 45 to 5 mol%. The acyloxy aromatic carboxylic acids mentioned here include P-acyloxybenzoic acid and/or 6-acyloxy-
2-naphthoic acid, such as P-acetoxybenzoic acid,
6-acetoxy-2-naphthoic acid and the like. If the amount of these acyloxy aromatic carboxylic acids used exceeds 50 mol % of the total, anisotropy (liquid crystal) will be exhibited, resulting in a highly anisotropic film or resin, which is not preferable. If it is less than 2 mol %, the effects of improving spinnability, fiber bending strength, film stretchability, and impact resistance, which are the objectives of the present invention, are small and the objectives of the present invention cannot be achieved.

本発明の共重合ポリエステルは最も好ましくは次の二段
階から製造される。まず第1段階ではポリエチレン−1
,2−ビス(2−クロルフェノキシ)エタン−4,4′
−ジカルボキシレート重合体にアシルオキシ芳香族カル
ボン酸を反応させて脱アシルオキシ酸を初期重合体とな
し、第2段階ではこの初期重合体の重縮合をさらに進め
て固有粘度を高め、目的とする共重合ポリエステルを得
るのである。
The copolyester of the present invention is most preferably produced in the following two steps. In the first step, polyethylene-1
,2-bis(2-chlorophenoxy)ethane-4,4'
- The dicarboxylate polymer is reacted with an acyloxyaromatic carboxylic acid to form a deacyloxy acid as an initial polymer, and in the second step, the initial polymer is further polycondensed to increase its intrinsic viscosity and produce the desired copolymer. Polymerized polyester is obtained.

第1段階の反応条件は常圧の不活性ガス雰囲気下に24
0〜320℃とくに250〜300℃に加熱し、脱離す
るアシルオキシ酸を積極的に除去する条件が採用される
。第1段階の反応温度が240℃以下では反応速度が遅
<、320℃以上では反応物の熱分解が起こる可能性が
あるため好ましくない。
The reaction conditions for the first stage were 24°C under an inert gas atmosphere at normal pressure.
Conditions are employed in which the acyloxy acid to be desorbed is actively removed by heating to 0 to 320°C, particularly 250 to 300°C. If the reaction temperature in the first stage is 240° C. or lower, the reaction rate is slow, and if it is 320° C. or higher, thermal decomposition of the reactants may occur, which is not preferable.

第2段階の反応条件は溶融状態の初期重合体をIMHg
以下の減圧下に290〜310℃に加熱する。短時間で
所望の固有粘度になるまで上昇させるため触媒を用いる
ことができる。特にこの方法に使われる代表的触媒には
酢酸ナトリウム、酢酸マグネシウム、酢酸ストロンチウ
ム、酢酸コバルト等の酢酸塩、三酸化アンチモン、テト
ラブチルチタネートなどを例示することができるが酢酸
ナトリウムが最も好ましい。使用する触媒量は一般にア
シルオキシ芳香族カルボン酸に対して0.0001〜0
.1重量%好ましくは0.001〜0.05重量%であ
る。
The reaction conditions for the second stage were to convert the initial polymer in the molten state into IMHg
Heat to 290-310° C. under reduced pressure. A catalyst can be used to increase the intrinsic viscosity to a desired value in a short period of time. In particular, typical catalysts used in this method include acetates such as sodium acetate, magnesium acetate, strontium acetate, and cobalt acetate, antimony trioxide, and tetrabutyl titanate, but sodium acetate is most preferred. The amount of catalyst used is generally from 0.0001 to 0 based on the acyloxyaromatic carboxylic acid.
.. 1% by weight, preferably 0.001-0.05% by weight.

かくして50〜98モル%の前記式(I)で示されるカ
ルボキシレート単位および50〜2モル%の前記式叫で
示されるカルボキシレート単位を有する本発明の共重合
ポリエステル重合ホリエステルは、オルソクロルフェノ
ール中(25℃)で測定した固有粘度が0.4〜12で
ある。
Thus, the copolyester polymerized polyester of the present invention having 50 to 98 mol% of the carboxylate units represented by the formula (I) and 50 to 2 mol% of the carboxylate units represented by the formula (I) has orthochlorophenol. The intrinsic viscosity measured at medium temperature (25°C) is 0.4 to 12.

本発明の共重合ポリエステルは融点が300℃以下と低
く、溶融流動性もすぐれているので、押出成形、射出成
形、圧縮成形、ブロー成形などの通常の溶融成形に供す
ることができ、繊維、フィルム、樹脂、容器、ホースな
どに加工することが可能であり、特にフィルムとして有
用である。
The copolymerized polyester of the present invention has a low melting point of 300°C or less and excellent melt fluidity, so it can be used for ordinary melt molding such as extrusion molding, injection molding, compression molding, and blow molding, and can be used to produce fibers and films. It can be processed into resins, containers, hoses, etc., and is particularly useful as a film.

なお成形時には本発明の共重合ポリエステルに対し、ガ
ラス繊維、炭素繊維、アスベストなどの強化剤、充填剤
、核剤、顔料、酸化防止剤、安定剤、可塑剤、滑剤、離
型剤などの添加剤や他の熱可塑性樹脂を添加して、成形
品に所望の特性を付与することができる。
During molding, reinforcing agents such as glass fibers, carbon fibers, and asbestos, fillers, nucleating agents, pigments, antioxidants, stabilizers, plasticizers, lubricants, mold release agents, etc. may be added to the copolymerized polyester of the present invention. Agents and other thermoplastic resins can be added to impart desired properties to the molded article.

本発明の共重合ポリエステルから得られる成形品は、 
強度や弾性率な どの機械的性質が極めてすぐれている。
The molded article obtained from the copolyester of the present invention is
It has extremely excellent mechanical properties such as strength and elastic modulus.

以下に実施例により本発明をさらに説明する。なお実施
例中の特性評価は次の規定に準じて行なった。
The present invention will be further explained below with reference to Examples. Note that the characteristics evaluation in the examples was performed according to the following regulations.

固有粘度−・−・オルソクロルフェノール(25℃)で
測定した。
Intrinsic viscosity: Measured using orthochlorophenol (25°C).

 7− mtmのヤング率・−−−ASTM D790繊維の屈
曲強度11・水分平衡とした単繊維30本を1テニール
当り200岬の荷重をか けて左右に角度60rpm往復運動 させ単繊維が屈曲摩擦部で切断し た時の回数を読みとり、30回切 断した時の回数の和を測定回数で 割った値を屈曲強度(回)とする。
7- Young's modulus of mtm---ASTM D790 bending strength of fiber 11・30 single fibers with moisture balance were reciprocated from side to side at an angle of 60 rpm with a load of 200 capes per 1 tenier, and the single fibers were bent at the frictional part. Read the number of times of cutting, and calculate the bending strength (times) by dividing the sum of the number of times of cutting 30 times by the number of times of measurement.

フィルムのヤング率・・・・ASTM D882フィル
ムのシャルピー衝撃強度−−−−ASTM D256延
伸速度は2.00(1/分で行な った。
Young's modulus of film: ASTM D882 Charpy impact strength of film: ASTM D256 Stretching speed was 2.00 (1/min).

溶 融 粘 度・・−・高化式フローテスターでずり速
度1000SeCで測定した。
Melt viscosity: Measured using a Koka type flow tester at a shear rate of 1000 SeC.

実施例1 固有粘度0.57のポリエチレン−1,2−ビ 8− ス(2−クロルフェノキシ)エタン−4,4’−ジカル
ボキシレート重合体2.78 峙(7モル)、P−アセ
トキシ安息香酸0.54 kg(3モル)および酢酸ナ
トリウム5,4fを攪拌機、蒸留塔および窒素ガス入口
を備えた反応器に仕込み窒素ガス雰囲気下260〜28
0℃で攪拌した。約1時間後、大部分の酢酸が留出し低
溶融粘度の共重合ポリエステル初期重合体が得られた。
Example 1 Polyethylene-1,2-bis(2-chlorophenoxy)ethane-4,4'-dicarboxylate polymer with an intrinsic viscosity of 0.57, 2.78 diagonals (7 mol), P-acetoxybenzoic acid 0.54 kg (3 mol) of acid and 5.4 f of sodium acetate were charged into a reactor equipped with a stirrer, a distillation column, and a nitrogen gas inlet, and the mixture was heated under a nitrogen gas atmosphere at 260 to 28 kg.
Stirred at 0°C. After about 1 hour, most of the acetic acid was distilled off, and a copolyester initial polymer with a low melt viscosity was obtained.

次に反応系を300℃に昇温すると同時に0、5 nH
gに減圧し、さらに4時間攪拌を続けた結果ベージュ色
不透明の固有粘度0,56のポリマが得られた。
Next, the temperature of the reaction system was raised to 300°C, and at the same time 0.5 nH
The pressure was reduced to 1.5 g, and stirring was continued for an additional 4 hours. As a result, a beige, opaque polymer with an intrinsic viscosity of 0.56 was obtained.

このポリマの理論構造式は次のとおりであり、このポリ
エステルの元素分析結果は第1表のとおり理論値とよい
一致を示した。
The theoretical structural formula of this polymer is as follows, and the elemental analysis results of this polyester showed good agreement with the theoretical values as shown in Table 1.

m / n (モル比)−30/70 第 1 表 ただし酸素含量(ホ)は(100%−6%−H%−01
%)から算出した。またこの共重合ポリエステルを偏光
顕微鏡の試料台にのせ、昇温して光学異方性の確認を行
なったが、等方性ポリマであることがわかった。またパ
ーキンエルマ社製DSC−I型を用いて10℃/分の昇
温速度で融点を測定した結果243℃であった。
m / n (molar ratio) - 30/70 Table 1 However, the oxygen content (e) is (100% - 6% - H% - 01
%). Furthermore, this copolymerized polyester was placed on a sample stage of a polarizing microscope and the temperature was raised to confirm the optical anisotropy, and it was found that it was an isotropic polymer. Further, the melting point was measured at a heating rate of 10°C/min using a PerkinElmer DSC-I model and found to be 243°C.

このポリマを180℃、3時間減圧乾燥した後300℃
でシート状に溶融押出しして未延伸フィルムを得た。こ
の未延伸フィルムを120℃で縦方向、横方向にそれぞ
れ3倍に同時二軸延伸せしめ200℃で1分間熱処理し
て二軸延伸フィルムを得り。
This polymer was dried at 180°C for 3 hours under reduced pressure and then heated to 300°C.
An unstretched film was obtained by melt extrusion into a sheet. This unstretched film was simultaneously biaxially stretched at 120° C. to 3 times the length in the machine direction and in the transverse direction, and heat treated at 200° C. for 1 minute to obtain a biaxially stretched film.

延伸時の最大延伸応力は0.47 kq /−とポリエ
チレン−1,2−ビス(2−クロルフェノキシ)エタン
−4,4′−ヒカルボキシレートの0、7 ky /−
よりもかなり低く延伸性の良好なことがわかった。また
、ヤング率は縦、横両方向とも650 kq、/ dと
かなり高く、シャルピー衝撃強度も45tg*n/−と
ポIJエチレンー1.2−ビス(2−クロルフェノキシ
)エタン−4,4′−ジカルボキシレートの25 ky
・tM/−よりもかなり高いことがわかった。
The maximum stretching stress during stretching was 0.47 kq/- and 0.7 ky/- for polyethylene-1,2-bis(2-chlorophenoxy)ethane-4,4'-hycarboxylate.
It was found that the stretchability was considerably lower than that of the above. In addition, the Young's modulus is quite high at 650 kq,/d in both the vertical and horizontal directions, and the Charpy impact strength is 45 tg*n/-, which is higher than that of PoIJ ethylene-1,2-bis(2-chlorophenoxy)ethane-4,4' 25 ky of dicarboxylate
- It was found to be considerably higher than tM/-.

実施例2 実施例Jと同じようにポリエチレン−1,2−ビス(2
−クロルフェノキシ)エタン−4,4′−ジカルボキシ
レートとP−アセトキシ安息香酸とから重合した第2表
に示すポリマ(固有粘度0.5〜0.6)を実施例1と
同じように溶融押出し未延伸フィルムを得た。この未延
伸ライlレムを120℃で同時二軸延伸せしめた後、た
だちに150〜240℃で1分 11− 間熱処理して二軸延伸フィルムをi’4 rこ。
Example 2 Polyethylene-1,2-bis(2
-chlorophenoxy)ethane-4,4'-dicarboxylate and P-acetoxybenzoic acid as shown in Table 2 (intrinsic viscosity 0.5 to 0.6) was melted in the same manner as in Example 1. An extruded unstretched film was obtained. This unstretched film was simultaneously biaxially stretched at 120°C, and then immediately heat-treated at 150 to 240°C for 1 minute to obtain a biaxially stretched film.

第2表から本発明の共重合ポリエステル番よ、溶融粘度
が低く延伸時の延伸応力も低0こと、ヤング率、シャル
ピー衝撃強度の高0こと力5わかる。
From Table 2, it can be seen that the copolymerized polyester of the present invention has a low melt viscosity, low stretching stress during stretching, and high Young's modulus and Charpy impact strength.

これに対して、本発明外のポリエステルL/lよ溶融粘
度が高かったり(実験I6)、延伸応力が高かったり(
実験46)、ヤング率力;低かったり(実験x5)、シ
ャフレビー衝撃強度の低いことがわかる(実験A6)。
On the other hand, the melt viscosity was higher (Experiment I6) and the stretching stress was higher (
Experiment 46), Young's modulus force was low (Experiment x5), and Schaffleby impact strength was low (Experiment A6).

 12− 実施例3 固有粘度0.57のポリエチレン−1,2−ビス(2−
クロルフェノキシ)エタン−4,4’−ジカルボキシレ
ート重合体3.58 kg(9モル)、6−アセトキシ
−2−ナフトイル酸0.23kg(1モル)および酢酸
ナトリウム6.91を攪拌機、蒸留塔および窒素ガス入
口を備えた反応器に仕込み窒素ガス雰囲気下250〜2
70℃で攪拌した。約1時間後火部分の酢酸が留出し低
溶融粘度の共重合ポリエステル初期重合体が得られた。
12- Example 3 Polyethylene-1,2-bis(2-
3.58 kg (9 mol) of chlorophenoxy)ethane-4,4'-dicarboxylate polymer, 0.23 kg (1 mol) of 6-acetoxy-2-naphthoic acid, and 6.91 kg of sodium acetate were added to a stirrer and a distillation column. and charged into a reactor equipped with a nitrogen gas inlet under a nitrogen gas atmosphere at 250~2
The mixture was stirred at 70°C. After about 1 hour, the acetic acid in the heated portion was distilled off, yielding a copolyester initial polymer with a low melt viscosity.

次に反応系を290℃に昇温すると同時に0、5 jl
lHgに減圧し、さらに4時間攪拌を続けた結果ベージ
ュ色不透明の固有粘度0.71のポリマが得られた。
Next, the temperature of the reaction system was raised to 290°C, and at the same time 0.5 jl
The pressure was reduced to 1Hg and stirring was continued for an additional 4 hours, resulting in a beige, opaque polymer with an intrinsic viscosity of 0.71.

このポリマの理論構造式は次のとおりであり、このポリ
エステルの元素分析結果は第3表のとおり理論値とよい
一致を示した。
The theoretical structural formula of this polymer is as follows, and the elemental analysis results of this polyester showed good agreement with the theoretical values as shown in Table 3.

 14− rn / n (モル比) = 10/90第 3 表 ただし酸素含量(4)+、1(100%−0%−H%−
CI96)から算出した。
14- rn / n (molar ratio) = 10/90 Table 3 However, oxygen content (4) +, 1 (100% - 0% - H% -
CI96).

このポリマを紡糸温度300℃、引取速度150m/分
で紡糸し、ビン温度100℃、熱板温度150℃で4.
9倍に延伸したところ251 f/dと高弾性率となり
、屈曲強度も460回とポリエチレン−1,2−ビス(
2−クロルフェノキシ)エタン−4,4’−ジカルボキ
シレートの160回よりもかなり良好であることがわか
った。
This polymer was spun at a spinning temperature of 300°C and a take-up speed of 150 m/min, and at a bottle temperature of 100°C and a hot plate temperature of 150°C.
When stretched 9 times, the elastic modulus was as high as 251 f/d, and the bending strength was 460 times, which is higher than that of polyethylene-1,2-bis(
It was found to be significantly better than 160 times for 2-chlorophenoxy)ethane-4,4'-dicarboxylate.

−17一-171

Claims (1)

【特許請求の範囲】 50モル%を越え98モル%以下の次式(I)で示され
るカルボキシレート単位 しl および50モル%未満2モル%以上の次式(Ilで示さ
れるカルボキシレート単位 1 (−OR(j (I) を示す)を有する共重合ポリエステル。
[Scope of Claims] More than 50 mol% and 98 mol% of carboxylate units represented by the following formula (I) 1 and less than 50 mol% and 2 mol% or more of carboxylate units represented by the following formula (I) A copolymerized polyester having -OR (indicating j (I)).
JP17639283A 1983-09-26 1983-09-26 Copolyester Pending JPS6067530A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17639283A JPS6067530A (en) 1983-09-26 1983-09-26 Copolyester

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17639283A JPS6067530A (en) 1983-09-26 1983-09-26 Copolyester

Publications (1)

Publication Number Publication Date
JPS6067530A true JPS6067530A (en) 1985-04-17

Family

ID=16012850

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17639283A Pending JPS6067530A (en) 1983-09-26 1983-09-26 Copolyester

Country Status (1)

Country Link
JP (1) JPS6067530A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0212944A2 (en) * 1985-08-13 1987-03-04 Kabushiki Kaisha Ueno Seiyaku Oyo Kenkyujo Melt-processable aromatic copolyester

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS491795A (en) * 1972-04-25 1974-01-09
JPS52139194A (en) * 1976-05-17 1977-11-19 Eastman Kodak Co Copolyester and preparation thereof
JPS5884821A (en) * 1981-11-16 1983-05-21 Asahi Chem Ind Co Ltd Copolyester fiber or film and preparation thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS491795A (en) * 1972-04-25 1974-01-09
JPS52139194A (en) * 1976-05-17 1977-11-19 Eastman Kodak Co Copolyester and preparation thereof
JPS5884821A (en) * 1981-11-16 1983-05-21 Asahi Chem Ind Co Ltd Copolyester fiber or film and preparation thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0212944A2 (en) * 1985-08-13 1987-03-04 Kabushiki Kaisha Ueno Seiyaku Oyo Kenkyujo Melt-processable aromatic copolyester

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