JP3047453B2 - Polyester resin compound - Google Patents
Polyester resin compoundInfo
- Publication number
- JP3047453B2 JP3047453B2 JP29860190A JP29860190A JP3047453B2 JP 3047453 B2 JP3047453 B2 JP 3047453B2 JP 29860190 A JP29860190 A JP 29860190A JP 29860190 A JP29860190 A JP 29860190A JP 3047453 B2 JP3047453 B2 JP 3047453B2
- Authority
- JP
- Japan
- Prior art keywords
- polyester
- acid
- ethylene terephthalate
- molding
- potassium
- 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 - Fee Related
Links
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は溶融成形した場合に低アルデヒド含有量で、
且つ高い透明性を有する成形物を得るに適したポリエス
テル樹脂配合物、さらに詳しくは、二軸延伸ブロー容器
用ポリエチレンテレフタレート系樹脂配合物を提供する
にある。DETAILED DESCRIPTION OF THE INVENTION (Industrial application field) The present invention has a low aldehyde content when melt-molded,
Another object of the present invention is to provide a polyester resin compound suitable for obtaining a molded product having high transparency, and more specifically, a polyethylene terephthalate resin compound for a biaxially stretched blow container.
ポリエチレンテレフタレート(以後PETと略記)は、
優れた機械的性質、熱的性質、電気的性質などにより商
業用途に広く使用されている。しかしながら、用途及び
需要拡大にともない、PETに要求される特性もそれぞれ
の用途分野において厳しくなっている。それらの要求特
性の一つとして、アルデヒド類の含有量が少なくて、且
つ白化の少ないPET成形品がある。Polyethylene terephthalate (hereinafter abbreviated as PET)
Due to its excellent mechanical, thermal, and electrical properties, it is widely used in commercial applications. However, with the expansion of applications and demands, the characteristics required for PET are becoming stricter in each application field. One of those required properties is a PET molded article having a low content of aldehydes and less whitening.
(従来の技術) 通常、工業的に行われている溶融重合法でPETを製造
すると、熱分解及び副反応等によってアセトアルデヒ
ド、クロトンアルデヒド、その他アルデヒドとグリコー
ルの反応物と考えられる1,3−ジメチルジオキソラン等
のアルデヒド類(以下種々のアルデヒドの反応物を単に
アルデヒド類と略称する。)が発生し、PET中に含有さ
れる。従って、アルデヒド類の含量が少ないことを要求
される用途分野では溶融重合樹脂を脱アルデヒド処理を
行わないでそのまま成形するとアルデヒド含量の少ない
成形品は得られない。従って、アルデヒド類の含量が少
ないことが要求される用途分野では、通常、固相重縮
合、あるいは長時間の乾燥処理によってアルデヒド類を
数ppmに低減化した樹脂が使用される。(Prior art) Usually, when PET is manufactured by a melt polymerization method that is industrially performed, acetaldehyde, crotonaldehyde, and other 1,3-dimethyl compounds that are considered to be reactants of aldehyde and glycol due to thermal decomposition and side reactions. Aldehydes such as dioxolane (hereinafter, various aldehyde reactants are simply referred to as aldehydes) are generated and contained in PET. Accordingly, in a field of application that requires a low content of aldehydes, a molded article having a low aldehyde content cannot be obtained by molding the molten polymer resin without dealdehyde treatment. Therefore, in an application field where the content of aldehydes is required to be low, a resin in which aldehydes are reduced to several ppm by solid-phase polycondensation or long-time drying treatment is usually used.
しかしながら、これらのアルデヒド類を低減化した樹
脂であっても、溶融成形時にアルデヒドが生成し増加す
る為、その後の成形品用途に悪影響を及ぼさぬ程度にま
で低減化することは困難である。そして、これらアルデ
ヒド類を含有したPET成形品、例えばボトルでは、アル
デヒド類は悪臭や異臭の原因となったり、内容物の風味
や香りを変えてしまい著しく商品価値を低下させる。
又、通常ポリエステルは成形時に白化を伴い、結晶化を
起こして不透明になり、成形品の商品価値を損ない易
い。この白化は、成形時のポリマー温度を上げることに
よりある程度防止できるが、温度を上げるとポリマーの
分解反応も促進することになり、成形前のポリマー中の
アルデヒド含有量を少なくしていても、成形時にアルデ
ヒドが大幅に増加してしまう。However, even with these resins in which aldehydes are reduced, aldehydes are generated and increased during melt molding, so that it is difficult to reduce them to such an extent that they do not adversely affect the use of molded articles thereafter. In the case of PET molded articles containing these aldehydes, for example, bottles, the aldehydes cause an unpleasant odor or an unpleasant odor, or change the flavor or aroma of the contents, thereby significantly lowering the commercial value.
Further, usually, polyester is accompanied by whitening at the time of molding, crystallizes, and becomes opaque, and the commercial value of the molded product is easily damaged. This whitening can be prevented to some extent by raising the polymer temperature at the time of molding, but increasing the temperature will also accelerate the decomposition reaction of the polymer, and even if the aldehyde content in the polymer before molding is reduced, molding Occasionally, aldehydes increase significantly.
(発明が解決しようとする課題) 成形品の白化及び成形時のアルデヒドの増加の防止を
同時に満足させる方法として、通常のポリエステルに第
三成分を共重合させて融点を下げさせたり、結晶性を小
さくすることにより、成形温度を下げて成形時のアルデ
ヒドの生成を抑制し、且つ、結晶化による白化を抑える
方法が知られている。しかしながら、これらの第三成分
を加えるのは、成形品の他の重要な要求特性である延伸
成形性、機械的強度、バリヤー性等を著しく損なうので
適切な方法でない。(Problems to be Solved by the Invention) As a method for simultaneously satisfying whitening of a molded article and prevention of an increase in aldehyde during molding, a third component is copolymerized with a normal polyester to lower the melting point or to improve the crystallinity. A method is known in which the molding temperature is lowered to suppress the generation of aldehyde during molding and to suppress whitening due to crystallization by reducing the size. However, the addition of these third components is not an appropriate method because it significantly impairs the other important required properties of the molded article, such as stretch formability, mechanical strength, and barrier properties.
アルデヒドは、エチレンテレフタレート単位から、熱
分解により生成するものであり、これを化学的に阻止す
る方法として末端ヒドロキシル基の減少、カルボキシル
基の増加等の方法が提案されている(特開昭53−28649
号公報、特開昭53−43796号公報)。しかしながら、こ
れらの方法はポリマー製造上複雑な作業を必要とし工業
的規模の操業に取り入れることは困難である。Aldehydes are produced by thermal decomposition from ethylene terephthalate units, and methods for chemically inhibiting this have been proposed, such as reducing the number of terminal hydroxyl groups and increasing the number of carboxyl groups (Japanese Patent Application Laid-Open No. Sho 53-53). 28649
JP-A-53-43796). However, these methods require complicated operations in polymer production and are difficult to incorporate into industrial-scale operations.
又、アルデヒド抑制剤としては特開昭58−157852号公
報の立体障害フェノール化合物、特公昭63−10740号公
報では、特殊な構成成分のポリエステルにアルカリ金属
化合物を金属として2〜20ppm添加含有させる方法が提
示されている。しかし、これらの方法によってもアルデ
ヒドの少ないことが要求される用途分野において低アル
デヒドで、かつ低ヘイズで高透明性の成形品を得ること
に関しては、充分満足されるとは言えない。Further, as the aldehyde inhibitor, a sterically hindered phenol compound disclosed in JP-A-58-157852, and JP-B-63-10740, a method of adding 2 to 20 ppm of an alkali metal compound as a metal to a polyester having a special constitutional component. Is presented. However, even with these methods, it cannot be said that obtaining a low-aldehyde, low-haze, and high-transparency molded article in an application field requiring a small amount of aldehyde is sufficiently satisfactory.
(課題を解決するための手段) 本発明者は、上記の点に留意し、ポリエステルの溶融
射出や押出成形時の熱分解によって生成するアルデヒド
を抑制し、かつ著しく透明性に優れた成形品を得るため
の添加剤を鋭意検討した結果、一次イオン化ポテンシャ
ルの低い金属化合物が効果があることを見いだし、さら
に特定の濃度の特定の高級脂肪酸のカリウム塩を溶融重
縮合終了後に添加配合することによって達成されること
を見出した。(Means for Solving the Problems) The present inventor has noted the above points, and has suppressed the aldehyde generated by the thermal decomposition at the time of melt injection or extrusion molding of polyester, and produced a molded article having extremely excellent transparency. As a result of intensive studies on additives to obtain, it was found that a metal compound having a low primary ionization potential was effective, and this was achieved by adding and compounding a potassium salt of a specific higher fatty acid at a specific concentration after completion of melt polycondensation. Found to be.
即ち、(A)エチレンテレフタレートを主たる繰り返
し単位とするポリエステルと(B)炭素数10〜32の脂肪
族モノカルボン酸のカリウム塩を前記(A)のポリエス
テル、或は、他のポリエステル樹脂と溶融混練りして得
られたマスターバッチからなる配合物、又は、(A)に
(B)をドライブレンドした配合物であって、該配合物
中の前記カリウム塩(B)の配合率がカリウム金属とし
て25〜85ppmであることを特徴とした2軸延伸ブロー容
器用ポリエステル樹脂配合物である。That is, (A) a polyester having ethylene terephthalate as a main repeating unit and (B) a potassium salt of an aliphatic monocarboxylic acid having 10 to 32 carbon atoms are melt-mixed with the polyester (A) or another polyester resin. A compound comprising a master batch obtained by kneading, or a compound obtained by dry blending (A) with (B), wherein the compounding ratio of the potassium salt (B) in the compound is as potassium metal. It is a polyester resin compound for a biaxially stretched blow container characterized by having a concentration of 25 to 85 ppm.
本発明のエチレンテレフタレートを主たる繰り返し単
位とするポリエステル(A)とは80mol%以上がエチレ
ンテレフタレートからなるものであるが、成形品の重要
な特性である延伸成形性、機械的強度、バリヤー性等の
特性に悪影響を与えないために97〜98mol%以上が望ま
しい。その共重合成分としてはイソフタル酸、p−β−
オキシエトキシ安息香酸、ジフェニルエーテル−4,4′
−ジカルボン酸、ジフェノキシエタン−4,4′−ジカル
ボン酸、アジピン酸、セバシン酸等のジカルボン酸成
分、プロピレングリコール、ブタンジオール、ネオペン
チルグリコール、シクロヘキサンジメタノール、ビスフ
ェノールAのエチレンオキサイド付加物等のグリコール
類である。The polyester (A) having ethylene terephthalate as a main repeating unit of the present invention is one in which 80 mol% or more of ethylene terephthalate is composed of ethylene terephthalate, and has important properties such as stretch moldability, mechanical strength, and barrier properties. 97 to 98 mol% or more is desirable so as not to adversely affect the characteristics. Isophthalic acid, p-β-
Oxyethoxybenzoic acid, diphenyl ether-4,4 '
Dicarboxylic acid, diphenoxyethane-4,4'-dicarboxylic acid, dicarboxylic acid components such as adipic acid, sebacic acid, propylene glycol, butanediol, neopentyl glycol, cyclohexane dimethanol, ethylene oxide adduct of bisphenol A, etc. Glycols.
上記のポリエステルは直接エステル化を経て重縮合を
行う方法、或はエステル交換反応を経て重縮合を行う方
法のどちらの方法でも得られるが、溶融重合法で得られ
たポリエステルを180〜250℃の温度で減圧或は不活性ガ
ス中で固相状態で重合する必要がある。この際、必要に
応じエステル化、エステル交換及び重縮合反応の触媒と
してMn、Zn、Co、Ge、Sb、Ti等の金属化合物の一種以上
を任意に選択使用できる。そして又、本発明のポリエス
テルは必要に応じて着色剤、紫外線吸収剤、帯電防止
剤、熱酸化防止剤、坑菌剤、滑剤等の添加剤を適宜の割
合で含有することが出来る。The above polyester can be obtained by either a method of performing polycondensation via direct esterification or a method of performing polycondensation via a transesterification reaction.However, the polyester obtained by the melt polymerization method has a temperature of 180 to 250 ° C. It is necessary to polymerize in a solid state at reduced pressure or in an inert gas at a temperature. At this time, if necessary, one or more metal compounds such as Mn, Zn, Co, Ge, Sb, and Ti can be arbitrarily selected and used as a catalyst for the esterification, transesterification, and polycondensation reactions. Further, the polyester of the present invention can contain additives such as a colorant, an ultraviolet absorber, an antistatic agent, a thermal antioxidant, an antibacterial agent, and a lubricant in an appropriate ratio, if necessary.
炭素数10〜32の脂肪族モノカルボン酸のカリウム塩と
は、カプリン酸、ラウリン酸、ミリスチン酸、パルチミ
ン酸、ステアリン酸、ベヘニン酸、モンタン酸、メリシ
ン酸、オレイン酸、リノール酸等の飽和及び不飽和脂肪
酸のカリウム化合物を言う。The potassium salt of an aliphatic monocarboxylic acid having 10 to 32 carbon atoms includes capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, behenic acid, montanic acid, melicic acid, oleic acid, oleic acid, linoleic acid, and the like. It refers to the potassium compound of unsaturated fatty acids.
炭素数10〜32の脂肪族モノカルボン酸のカリウム塩の
配合量は、実施例(表−1)に示すがカリウム金属とし
て40ppmでアルデヒド量は最低値を示し、カリウム金属2
5ppm未満では目標の成形品材質中のアルデヒド量10ppm
より少なくすることはできない。又、カリウム金属が85
ppm以上ではヘイズ値が10%より大きくなる。The amount of the potassium salt of an aliphatic monocarboxylic acid having 10 to 32 carbon atoms is shown in Examples (Table 1). The potassium metal is 40 ppm, and the aldehyde content is the lowest.
If less than 5 ppm, target aldehyde content in molded article material is 10 ppm
There can be no less. In addition, potassium metal is 85
Above ppm, the haze value is greater than 10%.
本発明の炭素数10〜32の脂肪族モノカルボン酸のカリ
ウム塩の配合及び添加方法は、成形前に直接ポリエステ
ルとドライブレンドするか、予めポリエステルに溶融混
練り押し出し機で練り込み、高濃度の炭素数10〜32の脂
肪族モノカルボン酸のカリウム塩のポリエステルを再ペ
レット化し、いわゆるマスターバッチ(以後MBと略記)
を作成して、成形前にMBをポリエステルに混合して使用
するものである。炭素数10〜32の脂肪族モノカルボン酸
のカリウム塩の添加時期がポリエステルのエステル化反
応、或は、エステル交換反応時、又、溶融重縮合反応時
に添加配合したのでは成形時のアルデヒド生成の抑制効
果は失われるだけでなくポリエステルを着色させたり、
結晶性を増大させる等の悪影響を及ぼす。The potassium salt of an aliphatic monocarboxylic acid having 10 to 32 carbon atoms according to the present invention may be dry-blended with polyester directly before molding or melt-kneaded with polyester beforehand and kneaded with an extruder to obtain a high concentration of potassium. Re-pelletized polyester of potassium salt of aliphatic monocarboxylic acid having 10 to 32 carbon atoms, so-called masterbatch (hereinafter abbreviated as MB)
Is prepared by mixing MB with polyester before molding. The addition of the potassium salt of the aliphatic monocarboxylic acid having 10 to 32 carbon atoms during the esterification reaction of the polyester, the transesterification reaction, or the melt polycondensation reaction may result in the formation of aldehyde during molding. Not only is the suppression effect lost, but it can also color the polyester,
It has adverse effects such as increasing crystallinity.
本発明によれば、パルミチン酸カリウム、ステアリン
酸カリウム等のポリエステルの融点よりも高い融点の化
合物を配合しても成形品の透明性が損なわれないばかり
か、成形品の厚みが5mmもの厳しい条件下でも透明性を
維持できることは全く驚くべきことである。According to the present invention, even if a compound having a melting point higher than the melting point of the polyester such as potassium palmitate and potassium stearate is blended, the transparency of the molded product is not impaired, and the thickness of the molded product is as severe as 5 mm. It is quite surprising that transparency can be maintained even underneath.
(実施例) 以下、本発明を実施例により詳しく説明する。なを、
実施例及び比較例に挙げた特性値の評価法、測定方法は
次の通りである。(Examples) Hereinafter, the present invention will be described in more detail with reference to examples. What
The evaluation methods and measurement methods of the characteristic values listed in the examples and comparative examples are as follows.
1.固有粘度(IV) フェノール/テトラクロロエタン=60/40重量比の混
合溶媒中、400mg/dlの濃度で30℃で測定した値より求め
た。1. Intrinsic viscosity (IV) It was determined from a value measured at 30 ° C. at a concentration of 400 mg / dl in a mixed solvent of phenol / tetrachloroethane = 60/40 weight ratio.
2.アセトアルデヒド 試料を2〜3mm角に切り、試料/蒸留水=1g/2mlを窒
素置換したガラスアンプルに入れて上部を溶封し、160
℃で2時間抽出処理を行い、冷却後抽出液中のアルデヒ
ドを高感度ガスクロマトグラフィーで測定し濃度をppm
で表示した。2. Acetaldehyde A sample is cut into 2-3 mm squares, and a sample / distilled water = 1 g / 2 ml is placed in a glass ampoule purged with nitrogen, and the upper part is sealed.
Extraction at 2 ° C for 2 hours. After cooling, the aldehyde in the extract was measured by high-sensitivity gas chromatography and the concentration was ppm.
Displayed with.
3.ヘイズ(霞度%) 射出成形によって得た肉厚が5mmのプレートをJIS−K6
714、K6717、K7105、ASTM D 1003に従って製作され
た東洋精機製作所製直読ヘイズメーターにより測定し
た。ヘイズの算出式は以下に示す。3. Haze (% haze) A plate with a thickness of 5 mm obtained by injection molding is JIS-K6
714, K6717, K7105, measured by a direct-reading haze meter manufactured by Toyo Seiki Seisaku-sho, manufactured according to ASTM D1003. The formula for calculating the haze is shown below.
実施例 1 テレフタル酸100部とテレフタル酸の2倍molのエチレ
ングリコールを加圧下でエステル化反応をした後二酸化
ゲルマニュウム0.014部、燐酸0.025部を添加し285℃減
圧下で固有粘度が0.600になるまで重縮合をして流水中
に抜き出してペレットを得、結晶化処理した後に210℃
の窒素気流下の雰囲気で固有粘度が0.750になるまで固
相重縮合をした。そして、この方法で得られた固有粘度
0.750、アルデヒド含有量3.5ppmのPETをステアリン酸カ
リウムとドライブレンドして射出成形機により285℃の
成形温度で5mm肉厚のプレートを成形し、ヘイズ=7
%、アルデヒド=7.0ppmの成形品を得た。 Example 1 After 100 parts of terephthalic acid and an esterification reaction of ethylene glycol having twice the mole of terephthalic acid were performed under pressure, 0.014 part of germanium dioxide and 0.025 part of phosphoric acid were added, and the intrinsic viscosity was reduced to 0.600 at 285 ° C. under reduced pressure. After polycondensation, withdrawn in running water to obtain pellets, after crystallization treatment 210 ° C.
Was subjected to solid-state polycondensation in an atmosphere under a nitrogen stream until the intrinsic viscosity became 0.750. And the intrinsic viscosity obtained by this method
A PET having a thickness of 0.750 and an aldehyde content of 3.5 ppm was dry-blended with potassium stearate, and a 5 mm-thick plate was molded at a molding temperature of 285 ° C. using an injection molding machine.
%, Aldehyde = 7.0 ppm.
実施例 2〜7、比較例 3〜14 実施例1.の方法で得られた固相重合樹脂を二軸押し出
し機により、280℃で滞留時間1分の条件下で2.0重量%
/PETの添加剤を混練りしステアリン酸カリウムのMBを得
る。次に、MBに対して固相重縮合で得られたPETを表−
1.の配合量になるように混合し射出成形機で成形温度28
5℃で5mm肉厚のプレートを成形した。結果は表−1.に示
す。Examples 2 to 7 and Comparative Examples 3 to 14 The solid-state polymerized resin obtained by the method of Example 1 was subjected to a twin-screw extruder at 280 ° C. under a condition of a residence time of 1 minute at 2.0% by weight.
Knead the additives of / PET to obtain MB of potassium stearate. Next, the PET obtained by solid-phase polycondensation for MB is shown in Table-
Mix to achieve the compounding amount of 1. and mold with an injection molding machine at a molding temperature of 28.
A plate having a thickness of 5 mm was formed at 5 ° C. The results are shown in Table-1.
比較例1は実施例1の方法で得られた固相重合樹脂を
添加剤無しで成形した。In Comparative Example 1, the solid-phase polymerized resin obtained by the method of Example 1 was molded without any additives.
比較例2.についてはエステル化反応が終了した後にス
テアリン酸Kを添加して実施例1.と同様な方法で溶融重
合、固相重合を行い肉厚5mmのプレートを成形したが成
形時のアルデヒド生成の抑制効果はなく、しかも、ヘイ
ズ値も非常に高い値となった。For Comparative Example 2, after the esterification reaction was completed, stearic acid K was added and melt polymerization and solid phase polymerization were performed in the same manner as in Example 1 to form a plate having a thickness of 5 mm. There was no effect of suppressing generation, and the haze value was also very high.
実施例及び比較例(表−1.)より明らかなように特定
の高級脂肪酸のK塩の添加を溶融重合以降にKとして25
〜85ppmすることにより成形品のアルデヒド量<10ppm、
5mm厚ヘイズ<10%の値を同時に満足できる。炭素数の
少ない有機酸との化合物、K以外のアルカリ金属の使
用、あるいは、上記の範囲外のK濃度であってはヘイズ
及びアルデヒド量を同時に満足させるすることが出来な
い。そして又、ステアリン酸Kであっても溶融重合以前
の添加では成形時のアルデヒドの抑制効果は失われる。As is clear from the Examples and Comparative Examples (Table-1), the addition of the K salt of the specific higher fatty acid was changed to 25 as K after the melt polymerization.
Aldehyde content of molded article <10 ppm
The value of 5 mm thickness haze <10% can be satisfied at the same time. The use of a compound with an organic acid having a small number of carbon atoms, the use of an alkali metal other than K, or the K concentration outside the above range cannot simultaneously satisfy the haze and aldehyde amounts. Further, even if K stearic acid is added before melt polymerization, the effect of suppressing aldehyde during molding is lost.
(発明の効果) 本発明のポリエステル樹脂配合物を使用して成形すれ
ば、低アルデヒドで、かつ著しく透明性に優れたポリエ
ステル成形品を得ることが可能である。しかもポリエス
テル樹脂は特殊な原料組成である必要がなく、通常のポ
リエチレンテレフタレートでも本願の目的を達成できる
のであり、工業的意義は大きい。 (Effect of the Invention) By molding using the polyester resin composition of the present invention, it is possible to obtain a polyester molded article having low aldehyde and extremely excellent transparency. In addition, the polyester resin does not need to have a special raw material composition, and ordinary polyethylene terephthalate can achieve the object of the present invention, which is of great industrial significance.
Claims (1)
り返し単位とするポリエステルと(B)炭素数10〜32の
脂肪族モノカルボン酸のカリウム塩を前記(A)のポリ
エステル、或は、他のポリエステル樹脂と溶融混練りし
て得られたマスターバッチからなる配合物、又は、
(A)に(B)をドライブレンドした配合物であって、
該配合物中の前記カリウム塩(B)の配合率がカリウム
金属として25〜85ppmであることを特徴とした2軸延伸
ブロー容器用ポリエステル樹脂配合物。1. The polyester of (A) or another polyester resin comprising (A) a polyester having ethylene terephthalate as a main repeating unit and (B) a potassium salt of an aliphatic monocarboxylic acid having 10 to 32 carbon atoms. And a compound consisting of a master batch obtained by melt-kneading, or
A composition obtained by dry blending (B) with (A),
A polyester resin composition for a biaxially stretched blow container, characterized in that the content of the potassium salt (B) in the composition is 25 to 85 ppm as potassium metal.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29860190A JP3047453B2 (en) | 1990-11-02 | 1990-11-02 | Polyester resin compound |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29860190A JP3047453B2 (en) | 1990-11-02 | 1990-11-02 | Polyester resin compound |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04170464A JPH04170464A (en) | 1992-06-18 |
JP3047453B2 true JP3047453B2 (en) | 2000-05-29 |
Family
ID=17861846
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP29860190A Expired - Fee Related JP3047453B2 (en) | 1990-11-02 | 1990-11-02 | Polyester resin compound |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3047453B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6911523B2 (en) * | 2003-07-17 | 2005-06-28 | Colormatrix Corporation | Method to decrease the aldehyde content of polyesters |
JP7398042B2 (en) * | 2019-09-06 | 2023-12-14 | 東洋紡株式会社 | Polyester film and its manufacturing method |
-
1990
- 1990-11-02 JP JP29860190A patent/JP3047453B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH04170464A (en) | 1992-06-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6191209B1 (en) | Polyester compositions of low residual aldehyde content | |
KR101889135B1 (en) | Molded product composed of polyester resin composition | |
JP6054946B2 (en) | Polybutylene terephthalate resin composition and molded body | |
US3819759A (en) | Polyester molding compositions with triaryl phosphate and a polyphenylene oxide or a polycarbonate of bisphenol a | |
EP1674528B1 (en) | Aliphatic polyester composition and moulded article | |
JP6728458B2 (en) | Polymer blend with furan polyester | |
JP6113941B1 (en) | Method for producing polybutylene terephthalate resin composition and method for producing polybutylene terephthalate resin molding | |
KR20130055234A (en) | Blend of polylactic acid resin and copolyester resin and articles using the same | |
EP3177664B1 (en) | Modified polybutylene naphthalate for improved performance and process of making thereof | |
EP1431344B1 (en) | Polyethylene terephthalate compositions | |
US8597750B2 (en) | Polyester resin composition, method for producing same and molded body | |
JP3047453B2 (en) | Polyester resin compound | |
TWI388601B (en) | Copolyester resin composition for profile extrusion molding and molded articles made from the same | |
TWI831977B (en) | Polyester resin blend | |
JP2003528158A (en) | Thermoplastic copolyester compositions modified with epoxide compounds | |
TW583264B (en) | Improved copolyester with improved extrusion processing and color for extrusion blow molding | |
JPS6241256B2 (en) | ||
JP6152989B2 (en) | Mixed pellet containing polyester pellet and resin composition | |
JPH05214235A (en) | Composition | |
JPH0421704B2 (en) | ||
JP6931201B2 (en) | Polyester resin composition | |
JP3678091B2 (en) | Method for producing branched thermoplastic polyester resin | |
JP2545281B2 (en) | Halogen-containing thermoplastic resin composition | |
JP2023119208A (en) | Drawdown inhibitor for polyester resin | |
JPH06212062A (en) | Polyester elastomer composition |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080324 Year of fee payment: 8 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090324 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090324 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100324 Year of fee payment: 10 |
|
LAPS | Cancellation because of no payment of annual fees |