JPH0347176B2 - - Google Patents
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- Publication number
- JPH0347176B2 JPH0347176B2 JP60120625A JP12062585A JPH0347176B2 JP H0347176 B2 JPH0347176 B2 JP H0347176B2 JP 60120625 A JP60120625 A JP 60120625A JP 12062585 A JP12062585 A JP 12062585A JP H0347176 B2 JPH0347176 B2 JP H0347176B2
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- JP
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- Prior art keywords
- bottle
- polyester
- formula
- internal volume
- glycol
- 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
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- Polyesters Or Polycarbonates (AREA)
Description
〔産業上の利用分野〕
本発明はポリエステルボトルに関し、更に詳し
くは、透明性、ガスバリア性および耐圧変形性の
優れた、食品或いは飲料用等の容器として有利に
使用し得るポリエチレンテレフタレートボトルに
関する。
〔従来技術〕
従来より熱可塑性ポリエステル、特にポリエチ
レンテレフタレート(以下PETと略す)を2軸
延伸吹込成形して得られるボトルは、機械的強
度、ガスバリア性、透明性、耐薬品性等に優れた
特性を有することから、飲料用、食品用或いは化
粧品用等の容器として広く使用されている。
しかしながら、かかるPETボトルを例えば炭
酸ガスを加圧溶解せしめた炭酸飲料容器として使
用した際に、保存期間が長期に及ぶと内容液中の
炭酸ガスが徐々に損失し、商品価値を低める欠点
を有する。
かかる欠点を改良する方法として、ガスバリア
性の優れた樹脂とPETとを積層化する方法、或
いは溶融混合せしめる方法等が種々提案されてい
る。しかしながらかかる方法によるボトルは、
PETとバリア樹脂との積層の場合層間接着力が
弱く剥離が生じる等の欠点があり、溶融混合せし
める方法ではボトルの透明性が低下する等の欠点
がある。更には、PETボトルを使用後、PETポ
リマーを他の用途に再利用する際、或いはボトル
成形過程で発生するリプロポリマーをボトル成形
に再使用する際に、PETポリマーとバリア樹脂
との分離が困難となり使用上支障をきたす等の欠
点がある。
〔発明の目的〕
本発明の目的は、上記の如き欠点の無い、透明
性、ガスバリア性および耐圧変形性の良好なボト
ルを提供することにある。
〔発明の構成〕
本発明者は、前記の如き欠点の無いポリエステ
ルボトルに関し鋭意研究の結果、特定のPETポ
リマーよりなり、特定の物性を持つボトルであれ
ば欠点を改善出来る事を見出し本発明に到達し
た。
即ち本発明は、主たる繰り返し単位がエチレン
テレフタレートである熱可塑性ポリエステル樹脂
からなり、その胴部肉薄部分が2軸配向したボト
ルにおいて、該ポリエステルの固有粘度(IV)
と、エチレンテレフタレート以外のジカルボン酸
及びグリコール成分の共重合割合(W(wt%))
とが()式の範囲であり、前記肉薄部の平均面
配向度が0.125以上、平均肉厚が0.35mm以上であ
るポリエステルボトルである。
IV≧0.02W2+0.02W+0.66 ……()式
(但し0.5≦W≦3.0)
本発明における熱可塑性ポリエステル樹脂は、
その主たるくり返し単位がエチレンテレフタレー
トから成り、例えばイソフタル酸、ナフタリンジ
カルボン酸、ジフエニルジカルボン酸、ジフエノ
キシエタンジカルボン酸、シフエニルエーテルジ
カルボン酸、ジフエニルスルホンジカルボン酸等
の如き芳香族ジカルボン酸;ヘキサヒドロテレフ
タル酸、ヘキサヒドロイソフタル酸等の如き脂環
族ジカルボン酸;アジピン酸、セバチン酸、アゼ
ライン酸等の如き脂環族ジカルボン酸;p−β−
ヒドロキシエトキシ安息香酸、ε−オキシカプロ
ン酸等の如きオキシ酸;等のテレフタル酸以外の
二官能性カルボン酸の1種以上、及び/又は例え
ばトリメチレングリコール、テトラメチレングリ
コール、ヘキサメチレングリコール、デカメチレ
ングリコール、ネオペンチルグリコール、ジエチ
レングリコール、1,1−シクロヘキサンジメタ
ノール、1,4−シクロヘキサンジメタノール、
2,2−ビス(4′−β−ヒドロキシエトキシフエ
ニル)プロパン、ビス(4′−β−ヒドロキシエト
キシフエニル)スルホン酸等のエチレングリコー
ル以外のジオールの1種以上を共重合成分として
含むものであり、その共重合割合(W(ポリマー
重量に対するwt%))と固有粘度(IV)とが
()式の範囲となるポリエステルである。
IV≧0.02W2+0.02W+0.66 ……()式
(但し0.5≦W≦3.0)
特に、()式の範囲のポリエステルが好まし
い。
IV≧0.02W2+0.07W+0.64 ……()式
(但し0.5≦W≦2.5)
IVが()式の範囲よりも低いと、ガスバリ
ア性の良好なボトルが得難い。またWが0.5より
も低いPETは結晶化速度が速過ぎるため、非晶
質のプリフオームが得られない。Wが3.0よりも
大きいPETは配向性が悪くなり、炭酸ガス加圧
時の変形が著しく増加する。
本発明のボトルは、胴部肉薄部分が平均面配向
度が0.125以上に2軸配向されかつ平均肉厚が
0.35mm以上である。平均面配向度(以下△navと
略す)はボトル胴部の軸方向屈折率(ny)、周方
向屈折率(nx)及び厚み方向屈折率(nz)の測
定結果より下方により求めた数値である。
△nav={(ny−nz)+(nx−nz)}/2
通常市販されている炭酸飲料容器は、△nav≒
0.120〜0.123であるが本発明は△nav≧0.125の高
配向度ボトルであり、好ましくは△nav≧0.128で
あるとボトルの耐圧変形性、ガスバリア性が著し
く改善される。
同様の理由により、胴部平均肉厚は0.35mm以
上、好ましくは0.38mm以上である。
また本発明のボトルは、ボトル内容積に対し、
95〜97vol%の水と、該水の容積に対し、0℃
1atmの状態で4.0倍容量相当の炭酸ガス(20℃の
場合の圧力約3.7Kg/cm2G)を充填し打栓したの
ち、40℃で10日間保存せしめた後、開封した際の
ボトルの内容積増加割合が3%以下であることが
好ましい。
本発明のボトルは例えば実質的に非晶質のプリ
フオームを配向度が前記範囲となる温度条件(例
えば90℃〜130℃)にて軸方向に延伸し、かつ横
方向に吹込膨脹せしめる事により得られる。
吹込成形の際の延伸倍率は軸方向に2倍以上、
横方向に3倍以上、面積倍率で6倍以上であるこ
とが好ましい。
更に本発明のボトルの好ましい形状は、胴部は
基本的には円筒状であるが、若干のリブによる装
飾的な変形を与えたものでも良い。また底部形状
は、球状の凸形のものが好ましい。
〔実施例〕
以下、実施例により本発明を詳述する。なお主
な物性値の測定条件は次の通りである。
(1) 固有粘度〔IV〕:
o−クロロフエノールを溶媒として35℃で測
定。
(2) 密度〔ρ〕:
四塩化炭素とn−ヘプタンより作成した密度
勾配管にて30℃にて測定。
(3) 配向度〔△n〕:
アツベ屈折率計に偏光板を装置し、容器から
切り取つたサンプルの厚さ方向及び平面方向の
屈折率を温度25℃でナトリウムのD線を用いて
測定し、両者の値の差を計算により求めた。
(4) ガラス転位温度〔Tg〕:
290℃で溶融したのち0℃まで急冷したサン
プルを示差熱量計(セイコー電子工業(株)製
DSC−20型を使用)により10℃/minの昇温速
度で測定。
実施例1〜9及び比較例1〜7
表−1に示すIV、DEG(ジエチレングリコー
ル)及びIA(イソフタル酸)を共重合成分として
含有するRETチツプを熱風乾燥機にて乾燥後、
バレル径36mmφ、8オンスの射出成形機(名機製
作所製DM−100型)ホツパーに供給し、ホツト
ランナー式2個取プリフオーム金型(外径24〜25
mmφ、全長175mm、胴部肉厚3.5mm、口部ネジ径28
mm)にてプリフオーム(重量49g)を成形した。
射出成形条件は、シリンダー設定温度260〜285
℃、ホツトランナー温度290℃、成形サイクル35
秒、金型冷却水温度15℃であつた。得られたプリ
フオームはいずれも透明性が良好で実質的に非晶
質(密度1.335〜1.338)のものであつた。
かくして得られたプリフオームを、2軸配向ブ
ロー成形機(シンシナテイミラクロン社製RHB
−L型機)にて吹込成形して外径82mm、全高275
mm、丸底、胴部円筒状の内容積約1045mlのPET
ボトルを得た。得られたボトルのIV、胴部平均
特性を表−1に示す。
表−1のボトルIVとボトル容積増加割合(△
V(%))とをDEG重量割合(1部IA重量割合を
加算)をパラメーターとしてFig1に図示した。
Fig1より△Vが2.5%、3.0%、3.5%及び4.0%と
なるIVとDEG割合との相関を読み取つた結果を
Fig2に図示した。Fig2のDEG%(W)とIVと
の相関式は下式で近似される。
△V=2.5%の場合
IV=0.02W2+0.07W+0.64
△V=3.0%の場合
IV=0.02W2+0.02W+0.66
△V=3.5%の場合
IV=0.015W2+0.015W+0.645
△V=4.0%の場合
IV=0.01W2+0.02W+0.62
該ボトル内に、水1000g、クエン酸14gを充填
し、ボトル内気相部を炭酸ガス(以下CO2と書
く)で置換したのち、ポリエチレン製肉薄袋内に
秤量してある重曹(NaHCO3)14gをボトル内
クエン酸水溶液と直接接触しない状態でボトル口
部内に挿入し、直ちにアルミニウム製キヤツプ
(ポリエチレン内張)で打栓した。打栓後ボトル
口部内に挿入した重曹とクエン酸水溶液とが十分
に混り合う様ボトルを振り混ぜ反応によりCO2を
発生せしめて、CO2を加圧溶解せしめた水溶液が
ボトル内に充填された状態とした。該CO2充填ボ
トルを40℃の雰囲気にて10日間保存した後、20℃
の雰囲気に移し、12時間経過後にボトル内CO2圧
力を測定した。次いでアルミニウム製キヤツプを
開栓し、直ちにボトル内容積を測定した。
測定結果を表−1に示す。
また同様にして、ボトルを40℃での保存日数を
変えボトル内CO2圧力変化を測定し、得られた結
果より、内圧が3.0Kg/cm2G以下となる保存日数
を測定した。結果を表−1に示す。
[Industrial Application Field] The present invention relates to a polyester bottle, and more particularly to a polyethylene terephthalate bottle that has excellent transparency, gas barrier properties, and pressure deformation resistance and can be advantageously used as a container for food or beverages. [Prior art] Bottles obtained by biaxial stretch blow molding of thermoplastic polyester, particularly polyethylene terephthalate (hereinafter abbreviated as PET), have excellent properties such as mechanical strength, gas barrier properties, transparency, and chemical resistance. Because of this, they are widely used as containers for beverages, foods, cosmetics, etc. However, when such a PET bottle is used, for example, as a container for carbonated beverages in which carbon dioxide gas is dissolved under pressure, if the storage period is prolonged, the carbon dioxide gas in the content liquid will gradually be lost, resulting in a drawback that the product value will be lowered. . Various methods have been proposed to improve this drawback, such as a method of laminating resins with excellent gas barrier properties and PET, or a method of melt-mixing them. However, the bottles produced by this method are
Lamination of PET and barrier resin has drawbacks such as weak interlayer adhesion and peeling, while melt-mixing methods have drawbacks such as reduced bottle transparency. Furthermore, after using a PET bottle, it is difficult to separate the PET polymer and barrier resin when reusing the PET polymer for other purposes, or when reusing repropolymer generated during the bottle molding process for bottle molding. This has drawbacks such as problems in use. [Object of the Invention] An object of the present invention is to provide a bottle that is free from the above-mentioned drawbacks and has good transparency, gas barrier properties, and pressure deformation resistance. [Structure of the Invention] As a result of intensive research into polyester bottles that do not have the above-mentioned defects, the present inventor discovered that the defects can be improved if the bottle is made of a specific PET polymer and has specific physical properties. Reached. That is, the present invention provides a bottle made of a thermoplastic polyester resin whose main repeating unit is ethylene terephthalate, and whose thin body portion is biaxially oriented.
and copolymerization ratio (W (wt%)) of dicarboxylic acid and glycol components other than ethylene terephthalate
is within the range of formula (), the average degree of plane orientation of the thin wall portion is 0.125 or more, and the average wall thickness is 0.35 mm or more. IV≧0.02W 2 +0.02W+0.66 ... Formula () (however, 0.5≦W≦3.0) The thermoplastic polyester resin in the present invention is
Its main repeating unit consists of ethylene terephthalate, and aromatic dicarboxylic acids such as isophthalic acid, naphthalene dicarboxylic acid, diphenyl dicarboxylic acid, diphenoxyethane dicarboxylic acid, diphenyl ether dicarboxylic acid, diphenyl sulfone dicarboxylic acid, etc.; Alicyclic dicarboxylic acids such as hydroterephthalic acid, hexahydroisophthalic acid, etc.; Alicyclic dicarboxylic acids such as adipic acid, sebacic acid, azelaic acid, etc.; p-β-
one or more difunctional carboxylic acids other than terephthalic acid, such as oxyacids such as hydroxyethoxybenzoic acid, epsilon-oxycaproic acid, and/or e.g. trimethylene glycol, tetramethylene glycol, hexamethylene glycol, decamethylene Glycol, neopentyl glycol, diethylene glycol, 1,1-cyclohexanedimethanol, 1,4-cyclohexanedimethanol,
Contains one or more diols other than ethylene glycol, such as 2,2-bis(4'-β-hydroxyethoxyphenyl)propane and bis(4'-β-hydroxyethoxyphenyl)sulfonic acid, as a copolymerization component. It is a polyester whose copolymerization ratio (W (wt% relative to the polymer weight)) and intrinsic viscosity (IV) fall within the range of formula (). IV≧0.02W 2 +0.02W+0.66 () formula (however, 0.5≦W≦3.0) Particularly preferred is a polyester within the range of () formula. IV≧0.02W 2 +0.07W+0.64 () formula (however, 0.5≦W≦2.5) When IV is lower than the range of () formula, it is difficult to obtain a bottle with good gas barrier properties. Furthermore, PET with a W lower than 0.5 crystallizes at too high a rate, making it impossible to obtain an amorphous preform. PET with a W larger than 3.0 has poor orientation and significantly increases deformation when pressurized with carbon dioxide gas. In the bottle of the present invention, the thin wall portion of the body is biaxially oriented with an average plane orientation degree of 0.125 or more, and the average wall thickness is
It is 0.35mm or more. The average plane orientation degree (hereinafter abbreviated as △nav) is a numerical value obtained from the measurement results of the axial refractive index (ny), circumferential refractive index (nx), and thickness direction refractive index (nz) of the bottle body. . △n av = {(n y − nz ) + (n x − nz )}/2 Usually commercially available carbonated drink containers have △n av ≒
0.120 to 0.123, but the present invention provides a highly oriented bottle with Δn av ≧0.125, and preferably Δn av ≧0.128, which significantly improves the pressure deformation resistance and gas barrier properties of the bottle. For the same reason, the average wall thickness of the body is 0.35 mm or more, preferably 0.38 mm or more. In addition, the bottle of the present invention has a
95 to 97 vol% water and 0°C for the volume of the water
After filling with 4.0 times the volume of carbon dioxide gas (pressure approximately 3.7 Kg/cm 2 G at 20°C) at 1 atm and sealing the bottle, store it at 40°C for 10 days. It is preferable that the internal volume increase rate is 3% or less. The bottle of the present invention can be obtained, for example, by stretching a substantially amorphous preform in the axial direction under temperature conditions such that the degree of orientation falls within the above range (for example, 90°C to 130°C), and then blowing and expanding it in the lateral direction. It will be done. The stretching ratio during blow molding is 2 times or more in the axial direction,
It is preferable that the area magnification is 3 times or more in the lateral direction and 6 times or more in area magnification. Furthermore, the preferred shape of the bottle of the present invention is that the body is basically cylindrical, but it may be decoratively deformed with some ribs. Moreover, the bottom shape is preferably spherical and convex. [Example] Hereinafter, the present invention will be explained in detail with reference to Examples. The measurement conditions for the main physical property values are as follows. (1) Intrinsic viscosity [IV]: Measured at 35°C using o-chlorophenol as a solvent. (2) Density [ρ]: Measured at 30°C using a density gradient tube made from carbon tetrachloride and n-heptane. (3) Degree of orientation [△n]: A polarizing plate was attached to an Atsube refractometer, and the refractive index in the thickness direction and plane direction of the sample cut from the container was measured at a temperature of 25°C using sodium D line. , the difference between the two values was calculated. (4) Glass transition temperature [Tg]: A sample melted at 290°C and then rapidly cooled to 0°C was measured with a differential calorimeter (manufactured by Seiko Electronics Co., Ltd.).
Measured using DSC-20 model) at a heating rate of 10℃/min. Examples 1 to 9 and Comparative Examples 1 to 7 After drying RET chips containing IV, DEG (diethylene glycol), and IA (isophthalic acid) as copolymerization components shown in Table 1 in a hot air dryer,
A barrel diameter of 36mmφ and 8oz injection molding machine (DM-100 model manufactured by Meiki Seisakusho) is supplied to the hopper, and a hot runner type 2-cavity preform mold (outer diameter 24 to 25
mmφ, total length 175mm, body wall thickness 3.5mm, mouth screw diameter 28
A preform (weighing 49 g) was molded using 3 mm).
Injection molding conditions are cylinder set temperature 260-285
℃, hot runner temperature 290℃, molding cycle 35
Second, the mold cooling water temperature was 15°C. All of the obtained preforms had good transparency and were substantially amorphous (density 1.335 to 1.338). The preform thus obtained was molded using a biaxially oriented blow molding machine (RHB manufactured by Cincinnati Milacron).
-Blow molded using an L-type machine, with an outer diameter of 82 mm and a total height of 275 mm.
mm, round bottom, cylindrical body volume approximately 1045ml PET
Got a bottle. Table 1 shows the IV and body average characteristics of the obtained bottles. Bottle IV and bottle volume increase rate (△
V (%)) is illustrated in Fig. 1 using the DEG weight ratio (adding 1 part IA weight ratio) as a parameter.
From Fig 1, the results of reading the correlation between IV and DEG ratio where △V is 2.5%, 3.0%, 3.5% and 4.0% are shown.
It is illustrated in Fig.2. The correlation formula between DEG% (W) and IV in Fig. 2 is approximated by the following formula. When △V=2.5% IV=0.02W 2 +0.07W+0.64 When △V=3.0% IV=0.02W 2 +0.02W+0.66 When △V=3.5% IV=0.015W 2 +0.015W+0. 645 When △V=4.0% IV=0.01W 2 +0.02W+0.62 The bottle was filled with 1000 g of water and 14 g of citric acid, and the gas phase inside the bottle was replaced with carbon dioxide gas (hereinafter referred to as CO 2 ). Afterwards, 14 g of baking soda (NaHCO 3 ) weighed in a thin polyethylene bag was inserted into the mouth of the bottle without direct contact with the citric acid aqueous solution inside the bottle, and the bottle was immediately capped with an aluminum cap (lined with polyethylene). . After capping, the bottle is shaken so that the baking soda and citric acid aqueous solution inserted into the mouth of the bottle are sufficiently mixed to generate CO 2 through a reaction, and the aqueous solution in which CO 2 is dissolved under pressure is filled into the bottle. state. After storing the CO 2 -filled bottle in an atmosphere of 40°C for 10 days, it was heated to 20°C.
After 12 hours, the CO 2 pressure inside the bottle was measured. Next, the aluminum cap was opened and the volume inside the bottle was immediately measured. The measurement results are shown in Table-1. In the same manner, the bottle was stored at 40° C. for different days and the CO 2 pressure change inside the bottle was measured, and from the obtained results, the number of storage days at which the internal pressure became 3.0 Kg/cm 2 G or less was determined. The results are shown in Table-1.
【表】
表−1より明らかな通り、本発明のボトルは比
較例に示したボトルに対し、CO2保存性が飛躍的
に向上する。[Table] As is clear from Table 1, the bottle of the present invention has significantly improved CO 2 storage stability compared to the bottle shown in the comparative example.
第1図は、ボトルPETのIV及びDEG等の共重
合比率と、CO2加圧下保存後のボトル内容積増加
割合との関係を測定した結果を示す図である。第
2図は、ボトル内容積増加が一定割合となるボト
ルIVとDEG等の共重合比率との関係をFig1の結
果より読み取り図示したものである。
FIG. 1 is a diagram showing the results of measuring the relationship between the copolymerization ratio of IV, DEG, etc. of bottle PET and the bottle internal volume increase rate after storage under CO 2 pressure. FIG. 2 shows the relationship between the bottle IV and the copolymerization ratio of DEG, etc., in which the bottle internal volume increases at a constant rate, based on the results of FIG. 1.
Claims (1)
トである熱可塑性ポリエステル樹脂からなり、そ
の胴部肉薄部分が2軸配向したボトルにおいて、
該ポリエステルの固有粘度(IV)と、テレフタ
ル酸以外の二官能性カルボン酸成分およびエチレ
ングリコール以外のグリコール成分の共重合割合
(W(wt%))とが()式の範囲であり、前記肉
薄部の平均面配向度が0.125以上、平均肉厚が
0.35mm以上であるポリエステルボトル。 IV≧0.02W2+0.02W+0.66 ……()式 (但し0.5≦W≦3) 2 ボトル内容積に対し、95〜97vol%の水を充
填し、該水に対し、0℃、1atmの状態で4.0倍容
量相当の炭酸ガスを充填せしめ打栓密封したボト
ルを40℃で10日間保存せしめた後、開封した際の
ボトル内容積増加割合が3%以下である、特許請
求の範囲第1項記載のポリエステルボトル。[Claims] 1. A bottle made of a thermoplastic polyester resin whose main repeating unit is ethylene terephthalate, and whose thin body portion is biaxially oriented,
The intrinsic viscosity (IV) of the polyester and the copolymerization ratio (W (wt%)) of a bifunctional carboxylic acid component other than terephthalic acid and a glycol component other than ethylene glycol are within the range of formula (), and the above-mentioned thin The average plane orientation degree of the part is 0.125 or more, the average wall thickness is
Polyester bottles that are 0.35mm or larger. IV≧0.02W 2 +0.02W+0.66 ...Formula () (however, 0.5≦W≦3) 2 Fill the bottle with 95 to 97 vol% of water to the internal volume, and add water to the bottle at 0°C and 1 atm. Claim 1, wherein the bottle is filled with carbon dioxide gas equivalent to 4.0 times its capacity, sealed and capped, and stored at 40°C for 10 days, and then the bottle internal volume increases by 3% or less when the bottle is opened. Polyester bottle as described in section.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60120625A JPS61278527A (en) | 1985-06-05 | 1985-06-05 | Polyester bottle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60120625A JPS61278527A (en) | 1985-06-05 | 1985-06-05 | Polyester bottle |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61278527A JPS61278527A (en) | 1986-12-09 |
| JPH0347176B2 true JPH0347176B2 (en) | 1991-07-18 |
Family
ID=14790856
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60120625A Granted JPS61278527A (en) | 1985-06-05 | 1985-06-05 | Polyester bottle |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61278527A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5442036A (en) * | 1994-09-06 | 1995-08-15 | Eastman Chemical Company | Branched copolyesters especially suitable for extrusion blow molding |
| JP5239480B2 (en) * | 2008-04-23 | 2013-07-17 | 東洋製罐グループホールディングス株式会社 | Polyethylene terephthalate bottle |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS584611B2 (en) * | 1976-04-14 | 1983-01-27 | 三井化学株式会社 | plastic containers |
| JPS535261A (en) * | 1976-07-06 | 1978-01-18 | Toray Industries | Oriented hollow transparent molded article |
| JPS5450595A (en) * | 1977-09-30 | 1979-04-20 | Teijin Ltd | Preform for polyester hollow article and its preparation |
| JPS5468381A (en) * | 1977-11-07 | 1979-06-01 | Teijin Ltd | Container made of polyester and method of making said container |
-
1985
- 1985-06-05 JP JP60120625A patent/JPS61278527A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61278527A (en) | 1986-12-09 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |