JPH01197522A - Preparation of polyester - Google Patents
Preparation of polyesterInfo
- Publication number
- JPH01197522A JPH01197522A JP2005588A JP2005588A JPH01197522A JP H01197522 A JPH01197522 A JP H01197522A JP 2005588 A JP2005588 A JP 2005588A JP 2005588 A JP2005588 A JP 2005588A JP H01197522 A JPH01197522 A JP H01197522A
- Authority
- JP
- Japan
- Prior art keywords
- polyester
- cyclic oligomer
- heating
- heating medium
- present
- 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
Landscapes
- Polyesters Or Polycarbonates (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明はポリエステルの環状オリゴマーを重合する際に
、熱媒体の存在下で行うことを特徴とする無色透明でか
つ不純物のないポリエステルの製造方法に関するもので
ある。Detailed Description of the Invention (Industrial Application Field) The present invention relates to a method for producing a colorless, transparent and impurity-free polyester, which is characterized in that the polymerization of a cyclic polyester oligomer is carried out in the presence of a heat medium. It is related to.
(従来の技術)
従来より、ポリエステル環状オリゴマーを重合するとき
は、ポリエステル環状オリゴマー単独を高温で加熱して
行なっていた。(Prior Art) Conventionally, when polyester cyclic oligomers are polymerized, the polyester cyclic oligomers alone have been heated at high temperatures.
(発明が解決しようとする課M)
従来の樺にポリエステル環状オリゴマーを単独で重合を
行なう場合、環状オリゴマーの融点が300″C以上あ
るため、重合を高温で行なう必要があり、その結果ポリ
エステルの分解や着色が起こり、品質のよいポリエステ
ルが得られないと言う欠点があった。(Problem M to be solved by the invention) When polymerizing a polyester cyclic oligomer alone in conventional birch, the melting point of the cyclic oligomer is 300"C or higher, so the polymerization must be carried out at a high temperature, and as a result, the polyester The drawback was that decomposition and coloration occurred, making it impossible to obtain high-quality polyester.
(yA題を解決するための手段)
本発明者らは、前記i!!題を解決するため、鋭意研究
した結果、遂に本発明を完成するに到った。(Means for solving the yA problem) The present inventors solved the i! ! In order to solve this problem, as a result of intensive research, we have finally completed the present invention.
すなわち本発明は、ポリエステル環状オリゴマーを熱媒
体の存在下に加熱することを特徴とするポリエステルの
製造方法である。That is, the present invention is a method for producing polyester, which is characterized by heating a polyester cyclic oligomer in the presence of a heat medium.
本発明において熱媒体とは、反応温度内で流体として扱
うことが出来、ポリエステルに対して不活性である熱的
に安定な有機化合物を意味し、芳香族炭化水素、脂肪族
炭化水素、脂環族炭化水素より選ばれた化合物の一種又
は二種以上の混合物である。具体的には、パラフィン、
アルキルフェニル、ジメチルビフェニル、テトラエチル
ビフェニル、ジエチルビフェニル、トリメチルビフェニ
ル、トリエチルビフェニル、トリプロビルビフエ Cニ
ル、シクロへキシルヘンゼン、水素化トリフェニル、ア
ルキルナフタレン、シクロへキシルビフェニル等であり
、本発明においては、ポリエステルを膨潤させる力曹容
解させない熱媒体が好ましく、特に水素化トリフェニル
、アルキルジフェニルが望ましい。これら熱媒体は公知
の方法、例えば蒸留などにより精製して使用してもよい
。In the present invention, the heat medium refers to a thermally stable organic compound that can be treated as a fluid within the reaction temperature and is inert to polyester, including aromatic hydrocarbons, aliphatic hydrocarbons, alicyclic hydrocarbons, etc. It is one kind or a mixture of two or more kinds of compounds selected from group hydrocarbons. Specifically, paraffin,
Alkylphenyl, dimethylbiphenyl, tetraethylbiphenyl, diethylbiphenyl, trimethylbiphenyl, triethylbiphenyl, triprobylbiphenyl, cyclohexylhenzene, hydrogenated triphenyl, alkylnaphthalene, cyclohexylbiphenyl, etc., and in the present invention, A heating medium that does not cause the polyester to swell is preferable, and hydrogenated triphenyl and alkyldiphenyl are particularly preferable. These heat carriers may be used after being purified by known methods such as distillation.
本発明において用いられるポリエステル環状オリゴマー
とは、芳香族ジカルボン酸又はその同族体とグリコール
類とから誘導され、通常は2ないし10量体を言い、は
とんどが2ないし5量体であり、中でも3量体が多くを
占めている。前記芳香族ジカルボン酸又はその同族体成
分としては、テレフタル酸、イソフタル1M2.6−ナ
フタレンジカルボン酸あるいはこれらの、メチル、エチ
ル、プロピルなどのアルキルエステルなどが挙げられ、
グリコール成分としては、エチレングリコール、プロピ
レングリコール、ブチレングリコールなどが挙げられる
。The polyester cyclic oligomer used in the present invention is derived from an aromatic dicarboxylic acid or its homologue and glycols, and is usually a dimer to a decamer, most of which is a dimer to a pentamer, Among them, trimers account for the majority. Examples of the aromatic dicarboxylic acid or its analog component include terephthalic acid, isophthalic 1M2.6-naphthalene dicarboxylic acid, or alkyl esters thereof such as methyl, ethyl, propyl, etc.
Examples of the glycol component include ethylene glycol, propylene glycol, butylene glycol, and the like.
次にポリエステル環状オリゴマーよりポリエステルを製
造する本発明方法を具体的に述べると、まず公知の方法
により得られたポリエステル環状オリゴマーを約500
μ以下に粉砕し、このポリエステル環状オリゴマー1g
に対して熱媒体を0.1〜1.Oml 、好ましくは0
.2〜0.8mlの割合で反応容器中に存在させ、常圧
、減圧又は加圧下約200〜300°Cで窒素ガス、ヘ
リウム、炭酸ガス等の不・活性ガス気流中で加熱するこ
とによって重合されポリエステルが得られる。なお本発
明方法は、触媒なしでも重合できることも特長の一つで
あるが、従来より公知の触媒を存在させておいても何ら
差し支えない。以上の方法によって得られたポリエステ
ルは熱媒体を含んでいるが、これはアセトン、ベンゼン
などの有機溶媒で抽出することができる。Next, to specifically describe the method of the present invention for producing polyester from a polyester cyclic oligomer, first, a polyester cyclic oligomer obtained by a known method is
1 g of this polyester cyclic oligomer crushed to less than μ
0.1 to 1. Oml, preferably 0
.. Polymerization is carried out by placing the mixture in a reaction vessel at a ratio of 2 to 0.8 ml and heating it at about 200 to 300 °C under normal pressure, reduced pressure, or increased pressure in a stream of inert gas such as nitrogen gas, helium, or carbon dioxide gas. Polyester is obtained. Although one of the features of the method of the present invention is that it can be polymerized without a catalyst, there is no problem even if a conventionally known catalyst is present. The polyester obtained by the above method contains a heat medium, which can be extracted with an organic solvent such as acetone or benzene.
(作用) 本発明における熱媒体の作用は次のようなものである。(effect) The action of the heat medium in the present invention is as follows.
重合反応系に熱媒体を加えることにより比較的低温で撹
拌が均一に行なわれ、さらに重合が進み粘度が高くなっ
た時点においても、攪拌が容易に行なえるため、従来の
様に高温加熱によるポリエルテルの分解や着色が押さえ
られるものと思われる。By adding a heating medium to the polymerization reaction system, stirring can be performed uniformly at a relatively low temperature, and even when the polymerization has progressed and the viscosity has increased, stirring can be performed easily. It is thought that decomposition and discoloration of the particles can be suppressed.
(実施例)
以下、本発明を実施例により具体的に説明するが本発明
はこれらに限定されるものではない。なお極限粘度はフ
ェノール/テトラクロルエタン−3/2の混合溶媒を用
い、30°Cで測定したものである。(Examples) Hereinafter, the present invention will be specifically explained with reference to Examples, but the present invention is not limited thereto. Note that the intrinsic viscosity was measured at 30°C using a mixed solvent of phenol/tetrachloroethane-3/2.
実施例1゜
公知の方法により得られたポリエチレンテレフタレート
環状オリゴマー(純度98%以上)を500μ以下に粉
砕し、このポリエチレンテレフタレート1!2状オリゴ
マー10gを反応容器に仕込み、さらに熱媒体として水
素化トリフェニル5dを仕込んだ。系内を窒素ガスで置
換し、窒素気流下に280°Cで1時間加熱溶融撹拌す
ることにより、無色透明なポリエチレンテレフタレート
が得られた。得られたポリマー中の水素化トリフェニル
をアセトンで抽出し、得られたポリマーの極限粘度を測
定したところ、0.83であった。Example 1 A polyethylene terephthalate cyclic oligomer (purity of 98% or more) obtained by a known method was pulverized to 500μ or less, 10 g of this polyethylene terephthalate 1!2 oligomer was charged into a reaction vessel, and a hydrogenated triglyceride was added as a heat medium. Phenyl 5d was added. By purging the system with nitrogen gas and heating, melting and stirring at 280° C. for 1 hour under a nitrogen stream, colorless and transparent polyethylene terephthalate was obtained. Hydrogenated triphenyl in the obtained polymer was extracted with acetone, and the intrinsic viscosity of the obtained polymer was measured and found to be 0.83.
実施例2゜
実施例1と同様にして粉砕したポリエチレンテレフタレ
ート[状オリゴマー10gを反応容器に仕込み、さらに
熱媒体としてトリエチルビフェニル10m1を仕込んだ
。系内を窒素ガスで置換し、窒素気流下に280°Cで
1時間加熱溶融攪拌することによって、無色透明なポリ
エチレンテレフタレートが得られた。得られたポリマー
中のトリエチルビフェニルをアセトンで抽出し、得られ
たポリマーの極限粘度を測定したところ、0.75であ
った。Example 2 10 g of polyethylene terephthalate oligomer pulverized in the same manner as in Example 1 was charged into a reaction vessel, and 10 ml of triethyl biphenyl was further charged as a heat medium. By purging the system with nitrogen gas and heating, melting and stirring at 280° C. for 1 hour under a nitrogen stream, colorless and transparent polyethylene terephthalate was obtained. Triethyl biphenyl in the obtained polymer was extracted with acetone, and the intrinsic viscosity of the obtained polymer was measured and found to be 0.75.
比較例1゜
実施例1と同様にして粉砕したポリエチレンテレフタレ
ート環状オリゴマー10gを反応容器に仕込み、系内を
窒素ガスで置換し、窒素気流下に280°Cで2時間加
熱溶融攪拌することによって、茶色の濁ったポリエチレ
ンテレフタレートが得られた。その極限粘度を測定した
ところ、0.46であった。Comparative Example 1 10 g of polyethylene terephthalate cyclic oligomer crushed in the same manner as in Example 1 was charged into a reaction vessel, the inside of the system was replaced with nitrogen gas, and the mixture was heated and melted and stirred at 280°C for 2 hours under a nitrogen stream. A brown, cloudy polyethylene terephthalate was obtained. The intrinsic viscosity was measured and found to be 0.46.
(発明の効果)
以上かかる構成よりなる本発明方法を採用することによ
り、比較的低温でしかも無触媒で重合できるため、得ら
れたポリエステルは無色透明で、かつ金属化合物などの
不純物が全くないと言う画期的なものであり、食品用途
、その他に応用分野が飛躍的に拡大でき、産業界に寄与
すること大である。(Effects of the Invention) By employing the method of the present invention having the above configuration, polymerization can be performed at a relatively low temperature and without a catalyst, so that the obtained polyester is colorless and transparent and completely free of impurities such as metal compounds. This is a groundbreaking product that can dramatically expand its application to food applications and other fields, and will greatly contribute to industry.
特許出願人 東洋紡績株式会社Patent applicant: Toyobo Co., Ltd.
Claims (1)
加熱することを特徴とするポリエステルの製造方法。(1) A method for producing polyester, which comprises heating a polyester cyclic oligomer in the presence of a heat medium.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2005588A JPH01197522A (en) | 1988-01-29 | 1988-01-29 | Preparation of polyester |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2005588A JPH01197522A (en) | 1988-01-29 | 1988-01-29 | Preparation of polyester |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH01197522A true JPH01197522A (en) | 1989-08-09 |
Family
ID=12016388
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2005588A Pending JPH01197522A (en) | 1988-01-29 | 1988-01-29 | Preparation of polyester |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01197522A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6593179B2 (en) | 1999-11-18 | 2003-07-15 | Mitsubishi Denki Kabushiki Kaisha | Method of manufacturing a semiconductor device |
-
1988
- 1988-01-29 JP JP2005588A patent/JPH01197522A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6593179B2 (en) | 1999-11-18 | 2003-07-15 | Mitsubishi Denki Kabushiki Kaisha | Method of manufacturing a semiconductor device |
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