JP2666502B2 - Polyester production method - Google Patents

Polyester production method

Info

Publication number
JP2666502B2
JP2666502B2 JP2010152A JP1015290A JP2666502B2 JP 2666502 B2 JP2666502 B2 JP 2666502B2 JP 2010152 A JP2010152 A JP 2010152A JP 1015290 A JP1015290 A JP 1015290A JP 2666502 B2 JP2666502 B2 JP 2666502B2
Authority
JP
Japan
Prior art keywords
polyester
ppm
antimony trioxide
content
color tone
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
JP2010152A
Other languages
Japanese (ja)
Other versions
JPH03215522A (en
Inventor
浩 薬師寺
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
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Filing date
Publication date
Application filed by Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP2010152A priority Critical patent/JP2666502B2/en
Publication of JPH03215522A publication Critical patent/JPH03215522A/en
Application granted granted Critical
Publication of JP2666502B2 publication Critical patent/JP2666502B2/en
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Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、色調を改善するとともにその安定化をはか
り、かつ黒色異物を減少したポリエステルであって、製
糸、製膜時の口金汚れの軽減をはかったポリエステルの
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 polyester which has improved color tone and stabilizes the color tone, and has reduced black foreign matter. And a method for producing polyester.

[従来の技術] ポリエチレンテレフタレートもしくはエチレンテレフ
タレートを主たる繰り返し構成単位とするポリエステル
は、繊維用、フィルム用等の各種の工業的用途において
極めて価値の高いものである。
[Prior Art] Polyethylene terephthalate or a polyester containing ethylene terephthalate as a main repeating structural unit is extremely valuable in various industrial uses such as for fibers and films.

かかるポリエステルは、各種の工業的用途に使用さ
れ、その用途によって要求される特性が異なる。フィル
ム用、繊維用ともに共通して要求される特性としては安
定した色調、黒色異物のないこと、製糸、製膜時の口金
汚れの少ないことである。色調の安定化は、重縮合反応
における温度条件の安定、真空度の安定、重合時間の安
定により図れるが、原料系、特に触媒となる三酸化アン
チモンの特性変動によるポリマ色調の変動は逆に温度、
真空などの条件で変えることにより対処せざるを得ない
状態である。温度、真空条件の変更は得られるポリエス
テルの他の品質へも影響を与えるため、かかる条件の変
更によって、色調を安定化することは困難である。
Such polyesters are used for various industrial uses, and required properties differ depending on the use. Properties commonly required for both film and fiber use include stable color tone, no black foreign matter, and low stains on the spinneret during spinning and film formation. The color tone can be stabilized by stabilizing the temperature conditions in the polycondensation reaction, stabilizing the degree of vacuum and stabilizing the polymerization time. ,
It is in a state where it has to be dealt with by changing under conditions such as vacuum. Since changes in the temperature and vacuum conditions affect other qualities of the obtained polyester, it is difficult to stabilize the color tone by changing the conditions.

また、得られたポリエステル中の黒色異物、口金汚れ
物は、その大半がSb金属を主たる構成成分とするもので
ある。かかる黒色異物が減少させる方法として、従来種
々の方法が提案されているが、顕著な改善効果がみられ
ないのが実状である。
In addition, most of the black foreign matter and the stain on the base in the obtained polyester have Sb metal as a main component. Conventionally, various methods have been proposed as a method for reducing such black foreign matter, but in reality, no remarkable improvement effect is observed.

例えば特開平1−185355号公報において、Biの含有量
を特定化した三酸化アンチモンを使用することにより紡
糸時または製膜時のろ過圧力上昇を改善し、且つ製品の
色調も良好となる提案がなされているが、この方法によ
り紡糸時、製膜時のろ過圧力上昇、製品特性、色調は改
善されるものの改善効果が安定せず、時としてポリエス
テルが黄色化し、色調不良を起こす欠点を有していた。
For example, in JP-A-1-185355, a proposal has been made to improve the filtration pressure rise during spinning or film formation by using antimony trioxide with a specified Bi content, and also to improve the color tone of the product. Although this method improves the filtration pressure during spinning and film formation, improves product properties and color tone during spinning and film formation, the effect of the improvement is not stable, and sometimes the polyester yellows, resulting in poor color tone. I was

[発明が解決しようとする課題] 本発明の目的は、色調が安定し黒色異物が少なく製
糸、製膜の行程の口金汚れが少ないポリエステルの製造
方法を提供することにある。
[Problems to be Solved by the Invention] An object of the present invention is to provide a method for producing polyester, which has a stable color tone, has few black foreign substances, and has a small stain on a spinneret in a process of yarn production and film formation.

[課題を解決するための手段] 前記した本発明の目的は、芳香族ジカルボン酸または
その低級アルキルエステルとグリコールとからポリエス
テルを製造するに際し、重合触媒として、三酸化アンチ
モンと、ビスマスおよびセレンの化合物であって、且
つ、トリエチレングリコール(以下TEGという)還元性
が1.7%以下、Bi元素の含有量が0.1ppm〜100ppm、Se元
素の含有量が1ppm〜30ppmである三酸化アンチモン系化
合物を用いることを特徴とするポリエステルの製造方法
によって達成することができる。
[Means for Solving the Problems] An object of the present invention described above is to produce a polyester from an aromatic dicarboxylic acid or a lower alkyl ester thereof and a glycol, and to use a compound of antimony trioxide, bismuth and selenium as a polymerization catalyst. And an antimony trioxide compound having a triethylene glycol (hereinafter referred to as TEG) reducing property of 1.7% or less, a Bi element content of 0.1 ppm to 100 ppm, and a Se element content of 1 ppm to 30 ppm. It can be achieved by a method for producing a polyester characterized by the following.

本願発明者らは、前記の問題を解決するために、ポリ
エステルの製造に使用する三酸化アンチモン系化合物中
に含まれるBi元素、Se元素の含有量と、三酸化アンチモ
ン系化合物をTEGに加熱溶解させた後一定時間熱処理し
た時に生成する粒子量とが、ポリエステルの色調安定性
や黒色異物の発生量、ならびに、製糸、製膜行程での口
金汚れと関係があることを見出し、本発明に到達した。
In order to solve the above-mentioned problems, the inventors of the present application have determined that the contents of the Bi element and the Se element contained in the antimony trioxide-based compound used in the production of polyester and the antimony trioxide-based compound are dissolved by heating in TEG. It has been found that the amount of particles generated when heat treatment is performed for a certain period of time after the formation has a relationship with the color tone stability of polyester and the amount of black foreign matter generated, as well as spinning and stains in a spinneret in a film forming process, and reached the present invention. did.

本発明における三酸化アンチモン系化合物のTEG還元
性の評価は次の方法で行う。
The evaluation of the TEG reducing property of the antimony trioxide compound in the present invention is performed by the following method.

すなわち、三酸化アンチモン系化合物5gを250gのTEG
に添加し、250℃〜270℃で2時間撹拌下で溶解したの
ち、冷却する前に、ろ紙(5Bタイプ)でろ過する。ろ過
後、100mlの6N HClでろ上物を洗浄し、さらに100mlのエ
チルアルコールで洗浄し、乾燥する。このろ上物の重量
を秤量し、使用した三酸化アンチモン系化合物に対する
重量百分率で表わし、TEG還元性とする。
That is, 5 g of the antimony trioxide compound was added to 250 g of TEG.
, And dissolved under stirring at 250 ° C to 270 ° C for 2 hours, and then filtered through a filter paper (5B type) before cooling. After filtration, the residue is washed with 100 ml of 6N HCl, further washed with 100 ml of ethyl alcohol, and dried. The weight of the filtered product is weighed and expressed as a percentage by weight with respect to the used antimony trioxide-based compound, which is defined as TEG reducibility.

本発明では、TEG還元性が1.7%以下、好ましくは1.5
%以下、特に好ましくは1.3%以下であり、Bi元素含有
量が、100ppm未満、好ましくは70ppm未満、特に好まし
くは50ppm未満であり、さらに、Seの元素含有量が30ppm
以下、5ppm以上、好ましくは20ppm以下、10ppm以上の三
酸化アンチモン系化合物触媒を用いる、TEG還元性が1.7
%を越えると、製造したポリエステルの色調が、黄色味
を帯び好ましくない。
In the present invention, the TEG reducing property is 1.7% or less, preferably 1.5% or less.
% Or less, particularly preferably 1.3% or less, and the Bi element content is less than 100 ppm, preferably less than 70 ppm, particularly preferably less than 50 ppm, and the Se element content is less than 30 ppm.
Below, 5 ppm or more, preferably 20 ppm or less, using an antimony trioxide compound catalyst of 10 ppm or more, TEG reducibility is 1.7
%, The produced polyester has a yellow tint, which is not preferable.

TEGの還元性が1.7%以下であってもBi元素の含有量が
100ppmを越えると色調が黒ずみ、また、黒色異物の発生
が多くなり好ましくない。一方0.1ppm未満となると色調
が黄味化して好ましくない。さらにBiの含有量は1〜50
ppmが好ましくない。またSe元素の含有量が30ppmを越え
る、あるいは1ppm未満であると色調が黄味化して好まし
くない。
Even if the reducibility of TEG is 1.7% or less, the content of Bi
If it exceeds 100 ppm, the color tone becomes dark, and the generation of black foreign matters increases, which is not preferable. On the other hand, if it is less than 0.1 ppm, the color tone becomes yellowish, which is not preferable. Further, the content of Bi is 1 to 50.
ppm is not preferred. If the content of the Se element exceeds 30 ppm or less than 1 ppm, the color tone becomes yellowish, which is not preferable.

すなわち、TEGの還元性と、Bi元素の含有量、Se元素
の含有量の3つの要件を同時に満足した三酸化アンチモ
ン系化合物を触媒として用いることよってはじめて本発
明の目的とするポリエステルが製造できるのである。
That is, since the antimony trioxide-based compound, which simultaneously satisfies the three requirements of the reducibility of TEG, the content of the Bi element, and the content of the Se element, can be used as the catalyst, the polyester intended for the present invention can be produced. is there.

本発明の三酸化アンチモン系化合物は、アンチモン元
素、Bi元素およびSe元素等の金属を単体あるいは化合物
の状態で含有する鉱石を、一般的な製法により加熱、融
解、蒸発させ発生する混合気体に空気あるいは酸素など
を大量に吹き込み酸化させた後、急冷し三酸化アンチモ
ンを主成分としたBi元素、Se元素を特定量含有する微粒
子を析出させる方法、あるいは、アンチモン元素含有鉱
石に、Bi元素およびSe元素含有化合物を添加混合し、加
熱、融解、蒸発させて得られた混合気体を酸化させる方
法で製造する。
The antimony trioxide-based compound of the present invention is an ore containing a metal such as antimony element, Bi element and Se element alone or in the form of a compound, heated, melted and evaporated by a general production method to form a mixed gas. Alternatively, a large amount of oxygen or the like is oxidized and then oxidized, and then quenched to precipitate fine particles containing a specific amount of Bi element and Se element containing antimony trioxide as a main component. It is manufactured by adding and mixing an element-containing compound, heating, melting, and evaporating a mixed gas obtained by oxidation.

上記製法で得られた三酸化アンチモン系化合物中のBi
元素およびSe元素含有量、および、TEG還元性を測定
し、本願発明に規定する範囲の三酸化アンチモン系化合
物を選択する。
Bi in the antimony trioxide-based compound obtained by the above process
The contents of the element and the Se element and the TEG reducibility are measured, and an antimony trioxide-based compound within the range specified in the present invention is selected.

本発明のポリエステルの製造方法は、従来、公知の方
法を採用することができる。
As a method for producing the polyester of the present invention, a conventionally known method can be employed.

例えばジメチルテレフタレート等のテレフタル酸の低
級アルキルエステルとエチレングリコールとを原料とし
てエステル交換反応を行った後、重縮合させる方法、ま
たは、テレフタル酸(以下TPAという)とエチレングリ
コール(以下EGという)とを原料としてエステル化反応
後、重縮合させる方法のいずれの方法を適用しても良
い。また、ポリエステルの製造方法は、回分式でも、連
続式でもよいし、一部連続式を用いた半連続式を採用し
てもよい。
For example, a method of subjecting a lower alkyl ester of terephthalic acid such as dimethyl terephthalate to a transesterification reaction with ethylene glycol as a raw material, followed by polycondensation, or a method of terephthalic acid (hereinafter referred to as TPA) and ethylene glycol (hereinafter referred to as EG) Any method of polycondensation after the esterification reaction as a raw material may be applied. The method for producing the polyester may be a batch method, a continuous method, or a semi-continuous method using a partially continuous method.

三酸化アンチモン系化合物の添加時期は、重縮合反応
開始前であるが、エステル交換反応またはエステル化反
応開始前の反応系に添加することもできる。
The antimony trioxide-based compound is added before the start of the polycondensation reaction, but may be added to the reaction system before the start of the transesterification reaction or the esterification reaction.

また三酸化アンチモン系化合物の添加方法も、粉体
状、(EG)のスラリ、(EG)に溶解した溶液のいずれの
場合でもよく、特に制限はない。
The method of adding the antimony trioxide-based compound may be any of a powder, a slurry of (EG), and a solution dissolved in (EG), and is not particularly limited.

本発明により製造するポリエステルは芳香族カルボン
酸またはその低級アルキルエステルとグリコールとから
製造されるポリエステルが好ましいが、イソフタル酸、
フタル酸、ジエチレングリコール等の二塩基酸や多価ア
ルコールを添加あるいは共重合したポリエステルであっ
てもよい。また目的に応じて、製造過程で炭酸カルシウ
ム、シリカ、酸化チタン等の不活性無機粒子を添加した
り、ポリエステル製造行程で添加した化合物の反応によ
る析出粒子、いわゆる内部粒子を含んだものでもよい。
また、ポリエステルの製造時に、通常、添加される公知
の改質剤、安定化剤を配合することができる。
The polyester produced according to the present invention is preferably a polyester produced from an aromatic carboxylic acid or a lower alkyl ester thereof and a glycol, but is preferably isophthalic acid,
Polyester to which a dibasic acid such as phthalic acid or diethylene glycol or a polyhydric alcohol has been added or copolymerized may be used. Depending on the purpose, inert particles such as calcium carbonate, silica and titanium oxide may be added in the production process, or particles containing so-called internal particles precipitated by the reaction of the compound added in the polyester production process may be used.
Further, at the time of producing the polyester, known modifiers and stabilizers which are usually added can be blended.

[実施例] 以下本発明を実施例により、さらに詳細に説明する。
なお、実施例中の三酸化アンチモンは三酸化アンチモン
系化合物を、部は重量部を表わす。また実施例中の各測
定値は、次の方法で求めた。
[Examples] Hereinafter, the present invention will be described in more detail with reference to Examples.
In the examples, antimony trioxide represents an antimony trioxide-based compound, and parts represent parts by weight. Each measured value in the examples was obtained by the following method.

A.三酸化アンチモン中のビスマス元素含有量 原子吸光法により求めた。A. Bismuth element content in antimony trioxide Determined by atomic absorption method.

B.酸化アンチモン中のセレン元素含有量 ICP法により求めた。B. Selenium content in antimony oxide Determined by ICP method.

C.固有粘度 O−クロロフェノールを溶媒として25℃で測定した。C. Intrinsic viscosity It measured at 25 degreeC using O-chlorophenol as a solvent.

D.黒色異物 ポリエステルを厚さ0.1mmの2軸延伸フィルムに成形
し、それを実体顕微鏡で拡大し、目視観察によりフィル
ム1g当りの個数で表わした。
D. Black foreign matter Polyester was formed into a biaxially stretched film having a thickness of 0.1 mm, which was enlarged by a stereoscopic microscope, and expressed by the number per 1 g of the film by visual observation.

E.ポリエステルの色調 チップ状のポリエステルをカラーマシン(スガ試験機
(株)製)で測定し、L、b値で示した。
E. Color Tone of Polyester Chip-like polyester was measured with a color machine (manufactured by Suga Test Instruments Co., Ltd.), and indicated by L and b values.

実施例1 TPA85.8部とEG38.5部を260℃で4時間エステル化反応
して得られたビス−β−ヒドロキシエチルテレフタレー
ト低重合体(以下BHTという)に、TEG還元性1.10%、Bi
元素含有量48ppm、Se元素含有量13ppmの三酸化アンチモ
ンを0.025部、トリメチルフォスフェート0.06部、酢酸
カルシウム0.12部を添加して、290℃で0.5mmHgの減圧下
に3時間10分重縮合反応せしめた。得られた重合体は、
b値が5.0、L値が41.0、固有粘度0.650、黒色異物は0
コ/gであった。このポリマーを製糸したところ、口金汚
れはほとんどなく、良好なポリエステル糸が得られた。
Example 1 To a bis-β-hydroxyethyl terephthalate low polymer (hereinafter referred to as BHT) obtained by subjecting 85.8 parts of TPA and 38.5 parts of EG to an esterification reaction at 260 ° C. for 4 hours, 1.10% of TEG reducing property, Bi
Add 0.025 parts of antimony trioxide with an element content of 48 ppm and Se element content of 13 ppm, 0.06 part of trimethyl phosphate, and 0.12 part of calcium acetate, and carry out polycondensation reaction at 290 ° C. under a reduced pressure of 0.5 mmHg for 3 hours and 10 minutes. Was. The resulting polymer is
b value is 5.0, L value is 41.0, intrinsic viscosity is 0.650, black foreign matter is 0
KO / g. When this polymer was formed into a yarn, a good polyester yarn was obtained with almost no die stain.

実施例2 実施例1において、添加する三酸化アンチモンをTEG
還元性0.95%、Bi元素含有量25ppmSe元素含有量20ppmの
ものに変えた以外は、実施例1と同様の方法で実施し
た。得られたポリエステルはb値5.2、L値41.5、固有
粘度0.618、黒色異物は1コ/gであった。このポリマー
を製膜した結果、口金汚れもなく、製膜性も良好であっ
た。
Example 2 In Example 1, the added antimony trioxide was TEG.
The procedure was carried out in the same manner as in Example 1 except that the reducing property was changed to 0.95%, the Bi element content was 25 ppm, and the Se element content was 20 ppm. The resulting polyester had a b value of 5.2, an L value of 41.5, an intrinsic viscosity of 0.618, and a black foreign matter of 1 / g. As a result of forming this polymer into a film, there was no stain on the die and the film forming property was good.

実施例3 ジメチルテレフタレート100部、(EG)70部に酢酸カ
ルシウム0.07部とTEG還元性1.20%、Bi元素含有量15pp
m、Se元素含有量17ppmの三酸化アンチモンを添加し、常
法に従ってエステル交換反応を行ったのち、亜リン酸0.
015部を添加して、過剰の(EG)を留出させ、ビス−β
−ヒドロキシエチルテレフタレートを得た。これを常法
に従って2時間5分重縮合せしめて得られたポリエステ
ルは、固有粘度0.615、b値5.1、L値40.8で、黒色異物
も0コ/gであった。このポリエステルを製糸したとこ
ろ、製糸性は良好で、口金汚れもなく良好であった。
Example 3 100 parts of dimethyl terephthalate, 70 parts of (EG), 0.07 part of calcium acetate, 1.20% of TEG reducibility, and 15 pp of Bi element content
m, antimony trioxide having a Se element content of 17 ppm was added, and a transesterification reaction was performed according to a conventional method.
015 parts was added to distill off excess (EG) and bis-β
-Hydroxyethyl terephthalate was obtained. The polyester obtained by subjecting this to polycondensation for 2 hours and 5 minutes according to a conventional method had an intrinsic viscosity of 0.615, a b value of 5.1, and an L value of 40.8, and the number of black foreign substances was 0 / g. When this polyester was formed into a yarn, the spinning property was good and the base was not stained.

実施例4 表1に示す三酸化アンチモンに変更したこと以外は実
施例3と同様の方法で実施した。得られたポリエステル
の特性は表1に併記したとおり良好な品質であった。
Example 4 It carried out by the same method as Example 3 except having changed into antimony trioxide shown in Table 1. The properties of the obtained polyester were good as shown in Table 1.

比較実施例1 実施例1において、三酸化アンチモンとして、TEG還
元性0.95%、Bi元素含有量、180ppmSe元素含有量7ppmの
三酸化アンチモンを用いること以外は実施例1と同様の
方法で実施した。得られたポリエステルの色は黒ずんで
おり、黒色異物も多かった。(表1) 比較実施例2、3 三酸化アンチモンとして、表1中のものを使用したこ
と以外は実施例1と同様の方法で実施した。得られたポ
リエステルは表1に示すとおり、色調は黄味で、黒色異
物も多いものであった。
Comparative Example 1 The same procedure as in Example 1 was carried out except that antimony trioxide having a TEG reducing property of 0.95%, a Bi element content and a 180 ppm Se element content of 7 ppm was used as antimony trioxide. The color of the obtained polyester was dark, and there were many black foreign substances. (Table 1) Comparative Examples 2 and 3 The same procedure as in Example 1 was carried out except that the antimony trioxide shown in Table 1 was used. As shown in Table 1, the obtained polyester had a yellow color tone and many black foreign substances.

比較実施例4〜7 三酸化アンチモンとして、表1に示すものを使用した
こと以外は実施例3と同様の方法で実施した。いずれの
場合も得られたポリエステルは品質的に不良なものであ
った。
Comparative Examples 4 to 7 The same procedures as in Example 3 were performed except that antimony trioxide shown in Table 1 was used. In each case, the obtained polyester was poor in quality.

[発明の効果] 本発明のポリエステル製造方法は、色調が良好でかつ
安定し、黒色異物が少ないポリエステルを得るのに好適
な方法である。また得られたポリエステルを製糸あるい
は製膜工程に適用すると口金の汚れが少なく、また色調
も安定した製品とすることができる。
[Effect of the Invention] The polyester production method of the present invention is a method suitable for obtaining a polyester having a good and stable color tone and a small amount of black foreign matter. In addition, when the obtained polyester is applied to a yarn-forming or film-forming process, a product with less stain on a die and a stable color tone can be obtained.

Claims (1)

(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低級アルキ
ルエステルとグリコールとからポリエステルを製造する
に際し、重合触媒として、三酸化アンチモンと、ビスマ
スおよびセレンの化合物であって、且つ、トリエチレン
グリコール還元性が1.7%以下、該Bi元素の含有量が0.1
ppm〜100ppm、該Se元素の含有量が1ppm〜30ppmである三
酸化アンチモン系化合物を用いることを特徴とするポリ
エステルの製造方法。
1. A process for producing a polyester from an aromatic dicarboxylic acid or a lower alkyl ester thereof and a glycol, wherein the polymerization catalyst is a compound of antimony trioxide, bismuth and selenium, and has a triethylene glycol reducing property. 1.7% or less, the content of the Bi element is 0.1%
A method for producing a polyester, comprising using an antimony trioxide-based compound having a content of Se of 1 ppm to 30 ppm and a content of the Se element of 1 ppm to 30 ppm.
JP2010152A 1990-01-18 1990-01-18 Polyester production method Expired - Lifetime JP2666502B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2010152A JP2666502B2 (en) 1990-01-18 1990-01-18 Polyester production method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2010152A JP2666502B2 (en) 1990-01-18 1990-01-18 Polyester production method

Publications (2)

Publication Number Publication Date
JPH03215522A JPH03215522A (en) 1991-09-20
JP2666502B2 true JP2666502B2 (en) 1997-10-22

Family

ID=11742304

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2010152A Expired - Lifetime JP2666502B2 (en) 1990-01-18 1990-01-18 Polyester production method

Country Status (1)

Country Link
JP (1) JP2666502B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7132383B2 (en) 2000-09-12 2006-11-07 Toyo Boseki Kabushiki Kaisha Polymerization catalyst for polyester, polyester produced with the same, and process for producing polyester
WO2007035250A2 (en) 2005-09-16 2007-03-29 Eastman Chemical Company Polyester composition containing aluminum and lithium catalysts and titanium nitride particles and having improved reheat
US7199212B2 (en) 2000-01-05 2007-04-03 Toyo Boseki Kabushiki Kaisha Polymerization catalyst for polyesters, polyesters produced with the same and process for producing polyesters

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05222180A (en) * 1992-02-17 1993-08-31 Fuji Photo Film Co Ltd Production of polyester
WO2001014448A1 (en) 1999-08-24 2001-03-01 Toyo Boseki Kabushiki Kaisha Polymerization catalysts for polyesters, polyesters produced with the same and process for production of polyesters
MXPA03007471A (en) 2001-02-23 2003-12-04 Toyo Boseki Polymerization catalyst for polyester, polyester produced with the same, and process for producing polyester.

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2605298B2 (en) * 1987-09-08 1997-04-30 東レ株式会社 Polyester composition and method for producing the same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7199212B2 (en) 2000-01-05 2007-04-03 Toyo Boseki Kabushiki Kaisha Polymerization catalyst for polyesters, polyesters produced with the same and process for producing polyesters
US7132383B2 (en) 2000-09-12 2006-11-07 Toyo Boseki Kabushiki Kaisha Polymerization catalyst for polyester, polyester produced with the same, and process for producing polyester
WO2007035250A2 (en) 2005-09-16 2007-03-29 Eastman Chemical Company Polyester composition containing aluminum and lithium catalysts and titanium nitride particles and having improved reheat

Also Published As

Publication number Publication date
JPH03215522A (en) 1991-09-20

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