JPH028026A - Heat resistant hollow vessel - Google Patents

Heat resistant hollow vessel

Info

Publication number
JPH028026A
JPH028026A JP63158960A JP15896088A JPH028026A JP H028026 A JPH028026 A JP H028026A JP 63158960 A JP63158960 A JP 63158960A JP 15896088 A JP15896088 A JP 15896088A JP H028026 A JPH028026 A JP H028026A
Authority
JP
Japan
Prior art keywords
polyethylene terephthalate
preform
methacrylic resin
pearl
molding
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
JP63158960A
Other languages
Japanese (ja)
Inventor
Yasunori Terajima
寺嶌 泰範
Masatoshi Miura
三浦 正壽
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.)
Mitsubishi Rayon Co Ltd
Original Assignee
Mitsubishi Rayon Co 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
Application filed by Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP63158960A priority Critical patent/JPH028026A/en
Publication of JPH028026A publication Critical patent/JPH028026A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D1/00Containers having bodies formed in one piece, e.g. by casting metallic material, by moulding plastics, by blowing vitreous material, by throwing ceramic material, by moulding pulped fibrous material, by deep-drawing operations performed on sheet material
    • B65D1/02Bottles or similar containers with necks or like restricted apertures, designed for pouring contents
    • B65D1/0207Bottles or similar containers with necks or like restricted apertures, designed for pouring contents characterised by material, e.g. composition, physical features

Landscapes

  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Containers Having Bodies Formed In One Piece (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:To obtain a heat resistant hollow vessel having a pearl-like surface gloss which has specific hot-water shrinkage factor by blow molding a composition in which the ratio of polyethylene terephthalate to methacrylic resin is specified. CONSTITUTION:Methacrylic resin to be used is mixed in a range of 1-20wt.% in polyethylene terephthalate resin. If it exceeds this range, its pearl-like surface gloss is scarcely generated, while if it exceeds 20wt.% or more, the mechanical properties of the obtained hollow vessel and particularly dropping impact strength is reduced. A preform is obtained by drying a composition composed of polyethylene terephthalate and methacrylic resin so that its water content is reduced to less than 0.01%, and then molding it by a normal injection or extrusion molding method. The vessel is obtained by blow molding the preform in a blowing mold heated to 120-190 deg.C, and its hot-water shrinkage factor is 3% or less.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、耐熱収縮性に優れたパール状表面光沢を有す
る中空容器に関するもので、さらに詳しくは果汁飲料等
の高温充填を可能にした中空容器に関するものである。
Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a hollow container having a pearl-like surface gloss with excellent heat shrinkage resistance, and more specifically, a hollow container that enables high-temperature filling of fruit juice drinks, etc. It concerns containers.

[従来の技術] 近年ガラス製容器の代替品として、プラスチック製容器
が用いられるようになってきている。
[Prior Art] In recent years, plastic containers have come to be used as a substitute for glass containers.

最近では、ポリエチレンテレフタレートが機成的性質、
耐薬品性に優れ、しかもポリ塩化ビニルの如き可望剤や
残存モノマーによる人体への影響がなく、またポリエチ
レン、ポリプロピレン等に比べ酸素、炭酸ガス等のガス
透過率が低いことから食料品、飲料品、化粧品等の容器
に大量に使用されるようになってぎた。
Recently, polyethylene terephthalate has been developed with mechanical properties,
It has excellent chemical resistance, and has no effect on the human body due to lubricating agents such as polyvinyl chloride or residual monomers, and has a lower gas permeability for oxygen, carbon dioxide, etc. than polyethylene, polypropylene, etc., so it is suitable for foods and beverages. It has come to be used in large quantities for containers for products, cosmetics, etc.

[発明が解決しようとする課題] しかしながら、従来はポリエチレンテレフタレートを主
たる成分とするプリフォームを二軸延伸ブローして得ら
れた中空容器は低温のブロー金型を用いるため結晶化度
が低く耐熱収縮性に劣り70℃付近以上で変形するため
、80〜95℃の高温での熱殺菌を必要とするような果
汁飲料は一旦冷却工程を経てから充填しなければならず
、作業性にも劣るという欠点を有する。このため、耐熱
収縮性に優れた容器の製造が望まれており、かかる容器
の耐熱収縮性を向上させる方法として、−旦成形した容
器を定長下において使用ポリマーのガラス転B温度以上
の温度で熱処理を施すことが)足案されている。
[Problems to be Solved by the Invention] However, conventional hollow containers obtained by biaxially stretching and blowing preforms containing polyethylene terephthalate as a main component have low crystallinity and poor heat shrinkage resistance due to the use of low-temperature blow molds. Fruit juice drinks that require heat sterilization at high temperatures of 80 to 95 degrees Celsius must go through a cooling process before being filled, which means they are less workable. It has its drawbacks. For this reason, it is desired to manufacture containers with excellent heat shrinkage resistance, and as a method for improving the heat shrinkage resistance of such containers, the following methods are used: It has been proposed that heat treatment be applied at

かかる方法において熱処理温度が100℃以下のような
低温の場合、あるいは100℃を超えるような高温でも
プリフォームの残存内部応力を充分に緩和する程熱処理
時間が長くない場合は、80℃以上の高温充填には耐え
られない。また100℃を超えるような高温でプリフォ
ームの残存内部応力を充分に緩和する程熱処理時間を長
くした場合は、ポリエチレンテレフタレートが結晶化し
ているが故に、高温充填は可能となるもののくもりのか
かった外観を有し、装飾性の面で欠点を有する。
In such a method, if the heat treatment temperature is low, such as 100 °C or less, or if the heat treatment time is not long enough to sufficiently relieve the residual internal stress of the preform even at a high temperature exceeding 100 °C, the heat treatment temperature is 80 °C or higher. It cannot withstand filling. In addition, if the heat treatment time is long enough to sufficiently relax the residual internal stress of the preform at a high temperature exceeding 100°C, high-temperature filling is possible but cloudy because the polyethylene terephthalate is crystallized. It has a poor appearance and has disadvantages in terms of decoration.

[課題を解決するための手段] 本発明者らはかかる現状に鑑み、鋭意研究を重ねた結果
ポリエチレンテレフタレートにメタクリル系樹脂を特定
量配合した樹脂組成物をブロー成形することにより、ポ
リエチレンテレフタレートの特徴である耐薬品性、ガス
バリヤ−性等の性質をそのまま保持し、かつ80℃を超
えるような液体の充填を可能にし、さらにパール状表面
光沢を有する耐熱性中空容器が得られることを見出し、
本発明に到達したのである。
[Means for Solving the Problems] In view of the current situation, the present inventors have conducted extensive research, and as a result of blow molding a resin composition in which a specific amount of methacrylic resin is blended with polyethylene terephthalate, the characteristics of polyethylene terephthalate can be improved. We have discovered that it is possible to obtain a heat-resistant hollow container that maintains properties such as chemical resistance and gas barrier properties, that allows filling of liquids at temperatures exceeding 80°C, and that also has a pearl-like surface gloss,
The present invention has been achieved.

即ち本発明は、ポリエチレンテレフタレート80〜99
ffl量%とメタクリル系樹脂1〜20重量%から成る
ポリエチレンテレフタレート樹脂組成物から得られるプ
リフォームをブロー成形した熱水収縮率が3%以下のパ
ール状表面光沢を有する耐熱性中空容器である。
That is, the present invention uses polyethylene terephthalate 80 to 99
This is a heat-resistant hollow container having a pearl-like surface gloss and a hot water shrinkage rate of 3% or less, which is obtained by blow molding a preform obtained from a polyethylene terephthalate resin composition consisting of a polyethylene terephthalate resin composition comprising 1% to 20% by weight of a methacrylic resin.

本発明において用いられるポリエチレンテレフタレート
は、テレフタル酸成分とエチレングリコール成分とを主
成分として構成されるものであるが、テレフタル酸成分
の一部がイソフタル酸、アジピン酸、セバシン酸、ナフ
タレン−1,4−もしくは−2,6−ジカルボン酸、ジ
フェニルエーテル−4,4′−ジカルボン酸等のジカル
ボン酸でエチレングリコールの一部がプロピレングリコ
ール、ブチレングリコール、ネオペンチルグリコール、
シクロヘキサンジメタツール、2.2−ビス(4−ヒド
ロキシフェニル)プロパン等のグリコールで置換された
共重合物であってもよい。
The polyethylene terephthalate used in the present invention is mainly composed of a terephthalic acid component and an ethylene glycol component, but a part of the terephthalic acid component is isophthalic acid, adipic acid, sebacic acid, naphthalene-1,4 - or - Dicarboxylic acids such as 2,6-dicarboxylic acid and diphenyl ether-4,4'-dicarboxylic acid, in which a portion of ethylene glycol is propylene glycol, butylene glycol, neopentyl glycol,
Copolymers substituted with glycol such as cyclohexane dimetatool and 2,2-bis(4-hydroxyphenyl)propane may also be used.

ポリエチレンテレフタレートはエステル交換反応又は直
接のエステル化反応によりテレフタル酸とエチレングリ
コールとを重縮合させる等、通常の重合法によって得る
ことができるが、この際ポリエチレンテレフタレートの
固有粘度[ηコを0.7〜1.4の範囲に設定すること
が好ましい。ここで、固有粘度の比較的低いものをさら
に通常の固相重合法により高くすることも可能である。
Polyethylene terephthalate can be obtained by ordinary polymerization methods such as polycondensation of terephthalic acid and ethylene glycol through transesterification or direct esterification. It is preferable to set it in the range of ~1.4. Here, it is also possible to increase the relatively low intrinsic viscosity by using a conventional solid phase polymerization method.

ポリエチレンテレフタレートの固有粘度[η]が0,7
未満のものを用いると得られる容器の落下衝撃強度、特
に低温の落下衝撃強度が著しく低下するため好ましくな
い、又、固有粘度[y+]が1.4以上のものを用いる
とプリフォームをブロー成形して、中空容器を得ようと
する際、成形加工性が著しく困難となり目的とする中空
容器とすることができない、なお、固有粘度[η]は、
フェノール/テトラクロロエタン子50150(重量比
)溶液中25℃で測定した溶液粘度から求めた。
The intrinsic viscosity [η] of polyethylene terephthalate is 0.7
If a material with an intrinsic viscosity [y+] of 1.4 or more is used, the drop impact strength of the resulting container, especially at low temperatures, will be significantly reduced, which is undesirable.If a material with an intrinsic viscosity [y+] of 1.4 or more is used, the preform will be difficult to blow mold. When trying to obtain a hollow container, the molding processability becomes extremely difficult and the desired hollow container cannot be obtained.In addition, the intrinsic viscosity [η] is
It was determined from the solution viscosity measured at 25°C in a phenol/tetrachloroethane 50150 (weight ratio) solution.

本発明において用いられるメタクリル系樹脂とは、メタ
クリル酸メチルの単独重合体、50モル%以上のメタク
リル酸メチルと他のビニル単量体との共重合体、又はこ
れら重合体の混合物であってもよい、メタクリル酸メチ
ルと共重合させる他のビニル−’0−Ex体としてはア
クリル酸メチル、アクリル酸エチル、アクリル酸ブチル
などのアクリル酸アルキルエステル類、アクリロニトリ
ル、メタクリロニトリル、スチレン、α−メチルスチレ
ンなどが挙げられる。メタクリル酸メチルの単独重合体
又はメタクリル酸メチルとアクリル酸メチルあるいはア
クリル酸エチルとの共重合体が特に好ましい。
The methacrylic resin used in the present invention may be a homopolymer of methyl methacrylate, a copolymer of 50 mol% or more of methyl methacrylate and another vinyl monomer, or a mixture of these polymers. Other vinyl-'0-Ex compounds to be copolymerized with methyl methacrylate include acrylic acid alkyl esters such as methyl acrylate, ethyl acrylate, and butyl acrylate, acrylonitrile, methacrylonitrile, styrene, and α-methyl. Examples include styrene. Particularly preferred are homopolymers of methyl methacrylate or copolymers of methyl methacrylate and methyl acrylate or ethyl acrylate.

本発明において用いられるメタクリル系樹脂は、ポリエ
チレンテレフタレート樹脂組成物中に1〜20fii%
の範囲で配合して用いられる。この範囲を逸脱した場合
には、パール状表面光沢が発現しにくく、しかもメタク
リル系樹脂の配合量が2011i量%を超える場合には
得られる中空容器の機械的性質、特に落下衝撃強度が低
下するので好ましくない ポリエチレンテレフタレートとメタクリル系樹脂とから
成るポリエチレンテレフタレート組成物を得る方法は、
ポリエチレンテレフタレート重合後のチップとブレンド
して押出したり、あるいは射出成形直前にホッパー内で
ブレンドする等いずれの方法を用いてもよい。
The methacrylic resin used in the present invention is 1 to 20% in the polyethylene terephthalate resin composition.
It is used in combination within the range of. If it deviates from this range, pearl-like surface gloss will be difficult to develop, and if the amount of methacrylic resin exceeds 2011i mass%, the mechanical properties of the resulting hollow container, especially the drop impact strength, will deteriorate. Therefore, the method for obtaining a polyethylene terephthalate composition consisting of polyethylene terephthalate and methacrylic resin is as follows:
Any method may be used, such as blending with chips after polyethylene terephthalate polymerization and extrusion, or blending in a hopper immediately before injection molding.

また本発明においては、本発明の目的を損なわない範囲
で結晶化促進、加工性向上等の目的で低分子物質を添加
したり、物性改質のために充填剤や強化剤等、耐熱性向
上のための抗酸化剤等、さらには着色剤等を添加するこ
とは何ら制限されるものではない。
In addition, in the present invention, low-molecular substances may be added for the purpose of promoting crystallization and improving processability within a range that does not impair the purpose of the present invention, and fillers and reinforcing agents may be added to improve heat resistance to improve physical properties. There is no limit to the addition of antioxidants and the like, as well as colorants and the like.

本発明におけるプリフォームはポリエチレンテレフタレ
ートとメタクリル系樹脂とから成る組成物を水分含有率
が0.01%未満になるまで乾燥した後、通常の射出成
形法又は押出成形法により得られる。また、有底プリフ
ォームでも無底プリフォームでもよい0本発明の中空容
器は、上述したプリフォームを120〜190℃に加熱
されたブロー成形型にブロー成形して得られた熱水収縮
率が3%以下のものである。この際のブロー成形法とし
ては特に限定されるものではないが、いわゆる二軸延伸
吹込成形法が特に好ましく、この方法は有底プリフォー
ムを延伸配向可能な温度範囲に保持して二軸延伸ブロー
することにより、延伸配向により強靭な中空容器とする
ことができる。
The preform in the present invention is obtained by drying a composition comprising polyethylene terephthalate and a methacrylic resin until the water content becomes less than 0.01%, and then using a conventional injection molding method or extrusion molding method. Further, the hollow container of the present invention, which may be a preform with a bottom or a preform without a bottom, has a hot water shrinkage rate obtained by blow molding the preform described above in a blow mold heated to 120 to 190°C. 3% or less. The blow molding method at this time is not particularly limited, but a so-called biaxial stretch blow molding method is particularly preferable. By doing so, a strong hollow container can be obtained due to the stretching orientation.

また、吹込成形型の温度は120〜190℃、好ましく
は150〜170℃に加熱する。型温が120℃未満で
あると充分結晶化した中空容器が得られず、80℃を超
えるような高温の液体を充填したとき、変形してしまい
、また型温が190℃を超えると中空容器を吹込成形型
から離型する際中空容器が変形しやすいため好ましくな
い。該方法により得られた中空容器の胴部の結晶化度は
30〜60%であることが好ましく、型温に応じた時間
だけブロー成形型に接触させることによって目的に適合
した中空容器を得ることが可能となる0本発明の中空容
器を得る方法は具体的にはフリフオームを引き続き行な
われるブロー延伸配向を可能にするために予め80〜1
60℃の温度範囲に保持する。プリフォームをこの温度
範囲に保持するには溶融成形して得た高温状態のプリフ
ォームを一旦室温程度に冷却した後赤外線ヒーターなど
の加熱ヒーターで当該プリフォームを回転させながら均
一に加熱する方法などを適宜用いる。
Further, the temperature of the blow molding mold is heated to 120 to 190°C, preferably 150 to 170°C. If the mold temperature is less than 120°C, a sufficiently crystallized hollow container will not be obtained, and it will deform when filled with a liquid at a high temperature exceeding 80°C, and if the mold temperature exceeds 190°C, the hollow container will not be formed. This is not preferable because the hollow container is easily deformed when it is released from the blow mold. The degree of crystallinity of the body of the hollow container obtained by this method is preferably 30 to 60%, and by contacting with a blow mold for a time depending on the mold temperature, a hollow container suitable for the purpose can be obtained. Specifically, the method for obtaining the hollow container of the present invention, which allows the free-forming to be 80 to 1
Maintain temperature range of 60°C. In order to maintain the preform within this temperature range, the high-temperature preform obtained by melt molding is once cooled to about room temperature, and then the preform is rotated and heated uniformly using a heating heater such as an infrared heater. Use as appropriate.

しかる後直ちにこのプリフォームを120〜190℃に
加熱されたブロー成形型内に装填し延伸ロッドにより縦
方向に延伸した後、あるいは該延伸と同時に圧縮空気、
窒素のような加熱流体により同方向に一気に吹込膨張さ
せ二軸延伸配向させ、さらに加熱されたブロー成形型に
接触させ結晶化させることによって目的とする中空容器
を得ることができる。
Immediately thereafter, this preform is loaded into a blow molding mold heated to 120 to 190°C and stretched in the longitudinal direction with a stretching rod, or simultaneously with the stretching using compressed air,
The desired hollow container can be obtained by blowing and expanding the material at once in the same direction with a heated fluid such as nitrogen to achieve biaxial stretching and orientation, and then bringing it into contact with a heated blow mold for crystallization.

[実施例] 以下、実施例により本発明を具体的に説明する。[Example] Hereinafter, the present invention will be specifically explained with reference to Examples.

実施例中の結晶化度は30℃の臭化ナトリウム水溶液の
密度勾配管にて求めた密度から次式により計算して求め
たものである。
The degree of crystallinity in the examples was calculated from the density determined in a density gradient tube of an aqueous sodium bromide solution at 30° C. using the following formula.

但し、X:結晶化度(%) d:サンプルの密度(g/am’ ) dc:ポリエチレンテレフタレート1oO%結晶の密度
 1.455g/am’ da:ポリエチレンテレフタレート100%非品の密度
 1.335g/cm’ dO:メタクリル系樹脂の密度 (g/cm3) Φ:メタクリル系樹脂のm全分率(−)熱水収縮率は次
のようにして求めたものである。即ち成形して得られた
ボトル容器を測定した後100℃の沸騰水をボトル容器
内に充填する。
where, cm' dO: Density of methacrylic resin (g/cm3) Φ: m total fraction (-) of methacrylic resin The hot water shrinkage rate was determined as follows. That is, after measuring the bottle container obtained by molding, boiling water at 100° C. is filled into the bottle container.

沸騰水を充填してから10分後に沸騰水を捨て再びボト
ル容器の容積を測定し熱水収縮率を次式により求めた。
Ten minutes after filling with boiling water, the boiling water was discarded, the volume of the bottle container was measured again, and the hot water shrinkage rate was determined using the following formula.

−B 熱水収縮率=      X100(%)但し、Aは1
00℃の沸騰水を充填する前のボトル容器の容積(ml
) Bは100℃の沸騰水を捨てた後のボトル容器の容積(
ml) また、落下試験による破壊高さは次のようにして求めた
ものである。即ち成形して得られたボトルに満杯の水を
充填しキャップを占めASTMD−2463−74C法
に従って0℃における落下試験を行い、破壊高さを求め
た。
-B Hot water shrinkage rate = X100 (%) However, A is 1
Volume of bottle container before filling with boiling water at 00℃ (ml)
) B is the volume of the bottle container after discarding the 100℃ boiling water (
ml) In addition, the fracture height by the drop test was determined as follows. That is, the molded bottle was filled with water, the cap was occupied, and a drop test was conducted at 0° C. according to the ASTM D-2463-74C method to determine the fracture height.

また、外観の観察は目視にて行なった。In addition, the appearance was visually observed.

実施例1〜2、比較例1〜5 固有粘度[η]=1.2ml/gのポリエチレンテレフ
タレート(以下PETと略する。)に25℃クロロホル
ム中で測定した固有粘度が0.4のポリメチルメタクリ
レート単独重合体(以下PMMAと略する。)が表に示
される量添加されたポリエチレンテレフタレート樹脂組
成物を用いて、射出成形機により、樹脂温度280℃、
金型温度20℃の成形条件で、外形25mm、内径19
mm、長さ130mmの有底円筒状プリフォームに成形
した6次にこのプリフォームを回転させながら赤外線ヒ
ーター装置内に入れてプリフォームの温度が120℃に
なるように均一に加熱した後表に示される温度に加熱さ
れた成形用ブロー金型内に挿入し圧縮窒素をプリフォー
ム内部に圧入し、延伸ブローを行って内部圧力を保持し
た状態で成形体とブロー金型とを15秒間接触させたの
ち面延伸倍率約8倍の中空容器を得た。得られたボトル
の結晶化度、熱水収縮率、落下試験による破壊高さ及°
び外観観察結果を表に示す。
Examples 1-2, Comparative Examples 1-5 Polyethylene terephthalate (hereinafter abbreviated as PET) with an intrinsic viscosity [η] of 1.2 ml/g and polymethyl with an intrinsic viscosity of 0.4 measured in chloroform at 25°C Using a polyethylene terephthalate resin composition to which methacrylate homopolymer (hereinafter abbreviated as PMMA) was added in the amount shown in the table, the resin temperature was 280°C using an injection molding machine.
Under molding conditions of mold temperature 20℃, outer diameter 25mm, inner diameter 19
The preform was molded into a bottomed cylindrical preform with a length of 130 mm and a length of 130 mm.Next, the preform was placed in an infrared heater while rotating and heated uniformly so that the temperature of the preform reached 120 °C. The preform is inserted into a blow mold heated to the indicated temperature, compressed nitrogen is injected into the preform, and the molded body is brought into contact with the blow mold for 15 seconds while maintaining the internal pressure by stretch blowing. A hollow container with a surface stretching ratio of about 8 times was then obtained. Crystallinity, hot water shrinkage rate, fracture height and drop test results of the resulting bottles
The table shows the results of surface and appearance observation.

[発明の効果] 本発明により、ポリエチレンテレフタレートの特徴であ
る耐薬品性ガスバリヤ−性等の性質をそのまま保持し、
かつ80℃を超えるような液体の充填が可能であるパー
ル状表面光沢を有する耐熱性中空容器を提供することが
可能となった。
[Effects of the Invention] According to the present invention, properties such as chemical resistance and gas barrier properties, which are characteristics of polyethylene terephthalate, are maintained as they are,
Moreover, it has become possible to provide a heat-resistant hollow container having a pearl-like surface gloss and capable of being filled with liquid at temperatures exceeding 80°C.

特許出願人 三菱レイヨン株式会社 代理人 弁理士 吉 澤 敢 夫Patent applicant: Mitsubishi Rayon Co., Ltd. Agent: Patent attorney Yoshizawa Takeo

Claims (1)

【特許請求の範囲】[Claims] ポリエチレンテレフタレート80〜99重量%とメタク
リル系樹脂1〜20重量%から成るポリエチレンテレフ
タレート樹脂組成物から得られるプリフォームをブロー
成形した熱水収縮率が3%以下のパール状表面光沢を有
する耐熱性中空容器。
A heat-resistant hollow body having a pearl-like surface gloss and a hot water shrinkage rate of 3% or less, which is obtained by blow molding a preform obtained from a polyethylene terephthalate resin composition consisting of 80 to 99% by weight of polyethylene terephthalate and 1 to 20% by weight of a methacrylic resin. container.
JP63158960A 1988-06-27 1988-06-27 Heat resistant hollow vessel Pending JPH028026A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63158960A JPH028026A (en) 1988-06-27 1988-06-27 Heat resistant hollow vessel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63158960A JPH028026A (en) 1988-06-27 1988-06-27 Heat resistant hollow vessel

Publications (1)

Publication Number Publication Date
JPH028026A true JPH028026A (en) 1990-01-11

Family

ID=15683113

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63158960A Pending JPH028026A (en) 1988-06-27 1988-06-27 Heat resistant hollow vessel

Country Status (1)

Country Link
JP (1) JPH028026A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05124091A (en) * 1991-11-07 1993-05-21 Kao Corp Compound for extrusion blow molding and container formed by extrusion blow molding
US5454994A (en) * 1993-07-09 1995-10-03 Bayer Aktiengesellschaft Process for the production of molded parts and fillings made of rigid and flexible polyurethane foams using differential activator concentrations
JP2001293167A (en) * 2000-04-17 2001-10-23 Nippon Pachinko Buhin Kk Resin molding product relating to pachinko game machine and game machine using the same
JP2017522199A (en) * 2014-05-29 2017-08-10 ザ プロクター アンド ギャンブル カンパニー Glossy article

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05124091A (en) * 1991-11-07 1993-05-21 Kao Corp Compound for extrusion blow molding and container formed by extrusion blow molding
US5454994A (en) * 1993-07-09 1995-10-03 Bayer Aktiengesellschaft Process for the production of molded parts and fillings made of rigid and flexible polyurethane foams using differential activator concentrations
JP2001293167A (en) * 2000-04-17 2001-10-23 Nippon Pachinko Buhin Kk Resin molding product relating to pachinko game machine and game machine using the same
JP2017522199A (en) * 2014-05-29 2017-08-10 ザ プロクター アンド ギャンブル カンパニー Glossy article

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