JPH0473696B2 - - Google Patents
Info
- Publication number
- JPH0473696B2 JPH0473696B2 JP62033358A JP3335887A JPH0473696B2 JP H0473696 B2 JPH0473696 B2 JP H0473696B2 JP 62033358 A JP62033358 A JP 62033358A JP 3335887 A JP3335887 A JP 3335887A JP H0473696 B2 JPH0473696 B2 JP H0473696B2
- Authority
- JP
- Japan
- Prior art keywords
- mold
- molded product
- panel
- container
- manufacturing
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/02—Combined blow-moulding and manufacture of the preform or the parison
- B29C49/06—Injection blow-moulding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/02—Combined blow-moulding and manufacture of the preform or the parison
- B29C2049/023—Combined blow-moulding and manufacture of the preform or the parison using inherent heat of the preform, i.e. 1 step blow moulding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2791/00—Shaping characteristics in general
- B29C2791/001—Shaping in several steps
Landscapes
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、胴部に容器内圧吸収用のパネル状凹
部が形成されているポリエステルボトルの製造方
法に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for manufacturing a polyester bottle, in which a panel-shaped recess for absorbing internal pressure of the container is formed in the body.
(従来技術)
ポリエチレンテレフタレートの如き熱可塑性ポ
リエステルの二軸延伸ブロー成形容器は、優れた
透明性や表面光沢を有すると共に、びんに必要な
耐衝撃性、剛性、ガスバリヤー性を有しており、
各種液体のびん詰容器として利用されている。(Prior art) Biaxially stretched blow-molded containers made of thermoplastic polyester such as polyethylene terephthalate have excellent transparency and surface gloss, as well as impact resistance, rigidity, and gas barrier properties necessary for bottles.
It is used as a container for bottling various liquids.
また、延伸ポリエステルボトルは、透明性、ガ
スバリヤー性と共にガス入り飲料に対する耐圧性
において、他のプラスチツク製ボトルに較べて著
しく優れているが、延伸成形温度が比較的低温
(80〜110℃)であり、かつ非延伸部分乃至低延伸
部分があるために耐熱性がないので、ホツトパツ
クする場合、充填温度は65℃以下でないと実用に
供し得ず、その形状保持性がなくなるという欠点
がある。 In addition, stretched polyester bottles are significantly superior to other plastic bottles in terms of transparency, gas barrier properties, and pressure resistance against gas-filled beverages, but the stretching and forming temperature is relatively low (80 to 110°C). In addition, since it has non-stretched parts or low-stretched parts, it has no heat resistance, so when hot-packing, it cannot be put to practical use unless the filling temperature is 65°C or lower, and it has the disadvantage of losing its shape retention.
この欠点を除去するために、ポリエステルボト
ルの非延伸部分(例えば口頚部)と延伸部分(例
えば胴部)の熱処理(ヒートセツト)を行なうこ
とが提案されている。 In order to eliminate this drawback, it has been proposed to heat-set the unstretched parts (for example, the neck and neck) and the stretched parts (for example, the body) of the polyester bottle.
二軸延伸ポリエステルの熱固定は、器壁が滑ら
かな容器の場合には、65℃程度の温度迄の範囲に
おいて熱変形を防止するという効果をもたらす。 Heat setting of biaxially oriented polyester has the effect of preventing thermal deformation at temperatures up to about 65° C. in the case of containers with smooth walls.
然しながら、二軸延伸ポリエステルボトルへの
熱間充填によるビン詰製品の製造においては、加
熱時の内容物の容積と冷却時における内容積との
間にかなり大きな容積変化があり、この容積変化
に対応して容器内外にかなりの圧力差を生じる。 However, in the production of bottled products by hot filling into biaxially oriented polyester bottles, there is a fairly large volume change between the volume of the contents when heated and the volume when cooled, and it is necessary to deal with this volume change. This creates a significant pressure difference between the inside and outside of the container.
これを防止するために、容器胴部に相対的に径
が小となつているパネル状凹部を一定間隔で配置
し、このパネル状凹部を容器内の圧力変化に応じ
て胴部径方向に膨脹及び収縮し得る機能をもたせ
ることが行われている。 In order to prevent this, panel-shaped recesses with relatively small diameters are arranged at regular intervals in the container body, and these panel-shaped recesses expand in the radial direction of the body in response to pressure changes inside the container. And, it is being made to have the function of being able to contract.
(従来技術の問題点)
上述したパネル部を有しているポリエステルボ
トルは、この様なパネル状凹部に対応するキヤビ
テイ表面を有する割型を用いて延伸ブロー成形す
ることにより製造されている。(Problems with the Prior Art) The polyester bottle having the panel portion described above is manufactured by stretch blow molding using a split mold having a cavity surface corresponding to such a panel-shaped recess.
然しながら、この様な製造方法で得られたポリ
エステルボトルにおいては、そのパネル状凹部の
肉厚とそれ以外の柱部分の肉厚が実質的に等し
く、パネル状凹部が特に変形し易い様な構造とな
つていない。 However, in the polyester bottle obtained by such a manufacturing method, the wall thickness of the panel-shaped recess is substantially equal to the wall thickness of the other column parts, and the panel-shaped recess has a structure in which it is particularly easy to deform. I'm not used to it.
従つて、該ボトルに内容物を熱間充填した際、
そのパネル状凹部以外の胴部においてもボトル内
圧の変化によつて変形を生じるため、容器として
の外観が著しく損なわれるという問題がある。 Therefore, when hot filling the bottle with the contents,
Since deformation also occurs in the body other than the panel-shaped recess due to changes in bottle internal pressure, there is a problem in that the appearance of the container is significantly impaired.
この様な問題は、ボトルに内容物を充填し、こ
れを加熱殺菌する場合にも同様に生じる。 Such a problem also occurs when a bottle is filled with contents and then heat sterilized.
(発明の目的)
従つて本発明は上述した問題点を解決すること
を技術的課題とするものであり、ボトル胴部に形
成されるパネル状凹部がボトル内圧の変化に応じ
て他の部分よりも極めて容易に変形し得る様な構
造となつている二軸延伸ポリエステルボトルの製
造法を提供することを目的とする。(Purpose of the Invention) Therefore, the technical object of the present invention is to solve the above-mentioned problems, and the panel-shaped recess formed in the bottle body is made to move more easily than other parts according to changes in the internal pressure of the bottle. It is an object of the present invention to provide a method for manufacturing a biaxially oriented polyester bottle having a structure that can be deformed very easily.
(問題点を解決するための手段)
本発明によれば、熱可塑性ポリエステルから形
成され且つ容器口頚部に対応する首部を有する有
底プリフオームを、ブロー金型内にて二軸延伸ブ
ロー成形し、相対的に径の大きい凸部が所定間隔
で胴部に形成されている形状の中間成形品を製造
し、次いでこの中間成形品の胴部に形成されてい
る凸部を反転させてパネル状凹部として最終容器
形状とすることを特徴とする二軸延伸ポリエステ
ルボトルの製造法が提供される。(Means for Solving the Problems) According to the present invention, a bottomed preform made of thermoplastic polyester and having a neck corresponding to the neck of a container is biaxially stretched blow-molded in a blow mold, An intermediate molded product having a shape in which convex portions with a relatively large diameter are formed on the body at predetermined intervals is manufactured, and then the convex portions formed on the body of this intermediate molded product are inverted to form panel-shaped concave portions. Provided is a method for producing a biaxially oriented polyester bottle, characterized in that the bottle is shaped into a final container shape.
(作用)
本発明においては、二軸延伸ブロー成形により
一度相対的に径の大きな凸部が胴部に形成されて
いる中間成形品を製造し、次いでこの凸部を反転
させてパネル状凹部とすることが顕著な特徴であ
る。(Function) In the present invention, an intermediate molded product in which a convex portion with a relatively large diameter is formed on the body portion is manufactured by biaxial stretch blow molding, and then this convex portion is reversed to form a panel-like concave portion. This is a notable feature.
即ち、ブロー成形により胴部に凸部を形成せし
めると、該部分は他の胴部分に比して膨脹度合が
大となる。この結果としてこの凸部の肉厚は他の
部分よりも薄くなるのである。 That is, when a convex portion is formed on the body by blow molding, the degree of expansion of this portion is greater than that of the other body portions. As a result, the wall thickness of this convex portion becomes thinner than that of other portions.
本発明によれば、かかる凸部を反転させてパネ
ル状凹部とするため、最終容器においてパネル状
凹部は薄肉のものとなり、容器内圧の変化に応じ
て変形し易い構造となり、この結果として熱間充
填や加熱殺菌に際しても良好に容器形状が保持さ
れるのである。 According to the present invention, since such a convex portion is inverted to form a panel-like recess, the panel-like recess in the final container has a thin wall and has a structure that is easily deformed according to changes in the internal pressure of the container. The container shape is well maintained during filling and heat sterilization.
(発明の好適態様)
本発明を以下添付図面に示す具体例に基づいて
説明する。(Preferred Embodiments of the Invention) The present invention will be described below based on specific examples shown in the accompanying drawings.
まず本発明の製造方法によつて製造すべきボト
ルの形状を第1図に示す。 First, FIG. 1 shows the shape of a bottle to be manufactured by the manufacturing method of the present invention.
このボトル(全体として1で表わす)は、胴部
2に一定間隔でパネル状凹部3が形成されてお
り、パネル状凹部3の間は柱部4が形成される。 This bottle (represented as 1 as a whole) has panel-shaped recesses 3 formed at regular intervals in a body 2, and pillars 4 are formed between the panel-like recesses 3.
即ち該ボトル1は、パネル状凹部3がボトル内
圧を吸収し、内圧に応じて適宜変形してボトル1
の外観を良好に保持するものである。 That is, in the bottle 1, the panel-shaped recess 3 absorbs the bottle internal pressure, deforms appropriately according to the internal pressure, and becomes the bottle 1.
The appearance of the product is maintained well.
容器素材
本発明において、熱可塑性ポリエステルとして
は、エチレンテレフタート単位を主体とする熱可
塑性ポリエステル、例えばPETやグリコール成
分としてヘキサヒドロキシリレングリコール等の
他のグリコール類の少量を含有せしめ或いは二塩
基酸成分としてイソフタル酸やヘキサヒドロテレ
フタル酸等の他の二塩基酸成分の少量を含有せし
めた所謂改質PET等が使用される。これらのポ
リエステルは、単独でも或いはナイロン類、ポリ
カーボネート或いはポリアリレート等の他の樹脂
とのブレンド物の形でも使用し得る。用いるポリ
エステルは、当然のことながら、フイルムを形成
するに足る分子量を有するべきである。Container Material In the present invention, the thermoplastic polyester is a thermoplastic polyester mainly containing ethylene tereftate units, such as PET, a glycol component containing a small amount of other glycols such as hexahydroxylylene glycol, or a dibasic acid component. As such, so-called modified PET containing a small amount of other dibasic acid components such as isophthalic acid and hexahydroterephthalic acid is used. These polyesters can be used alone or in the form of blends with other resins such as nylons, polycarbonates, or polyarylates. The polyester used should, of course, have a sufficient molecular weight to form a film.
有底プリフオーム
延伸ブロー成形に使用する有底プリフオーム
は、それ自体公知の任意の手法、例えば射出成形
法、パイプ押出成形法等で製造される。前者の方
法では、溶融ポリエステルを射出し、最終容器に
対応する口頚部を備えた有底プリフオームを非晶
質の状態で製造する。後者の方法はエチレン−ビ
ニルアルコール共重合体等のガスバリヤー性中間
樹脂層を備えた有底プリフオームの製造に有利な
方法であり、押出された非晶質パイプを切断し、
一端部に圧縮成形で口頚部を形成させると共に、
他端部を閉じて有底プリフオームとする。高温下
での蓋との係合、密封状態を良好に維持するため
に、容器口頚部となる部分のみを予じめ熱結晶化
させておくことができる。勿論、この熱結晶化は
以後の任意の段階で行なうこともできる。Bottomed Preform The bottomed preform used in stretch blow molding is manufactured by any method known per se, such as injection molding method, pipe extrusion molding method, etc. In the former method, molten polyester is injected to produce a bottomed preform in an amorphous state with a neck and neck corresponding to the final container. The latter method is advantageous for producing a bottomed preform with a gas barrier intermediate resin layer such as ethylene-vinyl alcohol copolymer, and involves cutting an extruded amorphous pipe,
While forming a mouth and neck part by compression molding on one end,
The other end is closed to form a bottomed preform. In order to maintain good engagement with the lid and sealing under high temperatures, only the portion that will become the mouth and neck of the container can be thermally crystallized in advance. Of course, this thermal crystallization can also be performed at any subsequent step.
二軸延伸ブロー成形
本発明の製造方法においては、第2−A図及び
第2−B図に示す様なキヤビテイ表面を有する割
型10を用いて、上述した有底プリフオームの二
軸延伸ブロー成形を行ない、その胴部に相対的に
径の大きい凸部20を有する中間成形品30を形
成せしめる。Biaxial stretch blow molding In the manufacturing method of the present invention, the above-mentioned bottomed preform is biaxially stretch blow molded using a split mold 10 having a cavity surface as shown in FIGS. 2-A and 2-B. An intermediate molded product 30 having a convex portion 20 having a relatively large diameter on its body is formed.
この中間成形品30においては、凸部20の膨
脹度合が他の部分よりも大であるため、その肉厚
は他の部分、例えば柱部分21のそれよりも薄く
形成されることになる。 In this intermediate molded product 30, since the degree of expansion of the convex portion 20 is greater than that of other portions, its wall thickness is formed to be thinner than that of other portions, for example, the column portions 21.
第2−A図に示す型内におけるプリフオームの
二軸延伸ブロー成形は、それ自体公知の条件で行
なわれ、例えば一般に90乃至130℃、特に100乃至
120℃の延伸温度に予備加熱されたプリフオーム
を、延伸棒により軸方向に引張延伸するととも
に、流体吹込みにより周方向に膨脹延伸すること
により行なわれる。 Biaxial stretch blow molding of the preform in the mold shown in FIG.
This is done by stretching a preform preheated to a stretching temperature of 120° C. in the axial direction using a stretching rod, and expanding and stretching it in the circumferential direction by blowing fluid.
またこの二軸延伸ブロー成形においては、前記
割型10は熱固定温度に加熱されており、この状
態で二軸延伸ブロー成形が行なわれ、形成された
中間成形品30は、内部に流体圧が印加された状
態で引き続き第2−A図及び第2−B図に示す割
型内に保持され、熱固定が行なわれる。 In this biaxial stretch blow molding, the split mold 10 is heated to a heat-setting temperature, and the biaxial stretch blow molding is performed in this state, and the formed intermediate molded product 30 has fluid pressure inside. The applied state is then held in the split mold shown in FIGS. 2-A and 2-B, and heat-setting is performed.
一般にこの中間成形品30の胴部対応型表面1
0aは、熱可塑性ポリエステルの融点よりも低い
熱固定温度、例えば120乃至230℃、特に150乃至
200℃の温度に維持するのがよく、一方肩部対応
型表面10b及び底部対応型表面10cは、肩部
及び底部の分子配向の程度が胴部のそれに比して
小さいことから、胴部対応型表面10aの温度よ
りも低く且つ白化温度よりも低い温度でしかも可
及的に高い温度に維持するのがよい。具体的な加
熱温度は、肩部対応型表面10bで70乃至140℃、
特に100乃至130℃の範囲がよく、また底部対応型
表面10cで70乃至140℃、特に80乃至120℃の範
囲がよい。 Generally, the body-compatible surface 1 of this intermediate molded product 30
0a is a heat setting temperature lower than the melting point of the thermoplastic polyester, for example 120 to 230°C, especially 150 to 230°C.
The temperature is preferably maintained at 200° C., while the shoulder-compatible surface 10b and the bottom-compatible surface 10c have a lower degree of molecular orientation in the shoulder and bottom regions than in the torso. It is preferable to maintain the temperature at a temperature lower than the temperature of the mold surface 10a, lower than the whitening temperature, and as high as possible. The specific heating temperature is 70 to 140°C for the shoulder compatible surface 10b;
In particular, the temperature range is preferably from 100 to 130°C, and the temperature at the bottom corresponding surface 10c is preferably from 70 to 140°C, particularly from 80 to 120°C.
この金型内での熱固定に必要な時間は、型表面
温度によつても相違するが一般に1乃至30秒間、
特に3乃至15秒間程度の時間で充分である。 The time required for heat setting in the mold varies depending on the mold surface temperature, but generally it is 1 to 30 seconds.
In particular, a time of about 3 to 15 seconds is sufficient.
凸部の反転
熱固定が行なわれた中間成形品30は、次いで
割型内から取り出され、冷却されるとともに、該
成形品30の胴部に形成されている凸部20の反
転が行なわれる。Reversal of Convex Portions The heat-set intermediate molded product 30 is then taken out from the split mold, cooled, and the convex portions 20 formed on the body of the molded product 30 are reversed.
即ち、該凸部20を反転させることによつて、
最終容器のパネル状凹部に対応する凹部を形成す
るものである。 That is, by inverting the convex portion 20,
A recess corresponding to the panel-shaped recess of the final container is formed.
この様な凸部20の反転は、例えば第3図に示
す様に、熱固定された中間成形品30を位置固定
した状態でその凸部20にそれぞれ対応して適当
なロツド40を押しつけて、該凸部を凹ませるこ
とによつて容易に行なうことができる。 Such reversal of the convex portions 20 can be carried out by, for example, pressing appropriate rods 40 corresponding to the convex portions 20 with the heat-set intermediate molded product 30 fixed in position, as shown in FIG. This can be easily done by recessing the convex portion.
かくしてパネル状凹部が形成され、該凹部は他
の部分に比して薄肉となつている。 A panel-like recess is thus formed, and the recess has a thinner wall than other parts.
また冷却は型から取り出された成形品の過度の
変形を防止するために行なわれるが、形態及び寸
法の安定という見地から、上記反転操作の前に行
なうことが好適である。 Cooling is performed to prevent excessive deformation of the molded product taken out from the mold, but from the standpoint of stability of shape and dimensions, it is preferable to perform cooling before the above-mentioned inversion operation.
冷却の程度は、一般に成形品胴部の温度が胴部
対応型表面の温度よりも3乃至40℃低い温度、特
に5乃至30℃低い温度となる様に冷却するのがよ
い。この冷却はブロー成形金型から前記反転操作
域若しくは後述の二次ブロー成形域に成形品を移
送する際に、室温の空気雰囲気に曝露し放冷によ
つて行なうか、或いはブロー金型から取り出した
成形品に冷風を積極的に吹き付けることによつて
行なうことができる。また冷却金型にこれを入れ
て膨脹下に行なうこともできる。冷却金型を用い
る場合には以下の二次ブロー成形は必要でない。 The degree of cooling is preferably such that the temperature of the body of the molded article is generally 3 to 40°C lower, particularly 5 to 30°C lower than the temperature of the surface of the mold corresponding to the body. This cooling is performed either by exposing the molded product to an air atmosphere at room temperature and allowing it to cool when transferring the molded product from the blow molding mold to the above-mentioned reversal operation area or the secondary blow molding area described below, or by cooling the molded product by exposing it to an air atmosphere at room temperature, or by removing it from the blow mold. This can be done by actively blowing cold air onto the molded product. Alternatively, it can be placed in a cooling mold and subjected to expansion. When using a cooling mold, the following secondary blow molding is not necessary.
二次ブロー成形
冷却され且つ所定のパネル状凹部が形成された
成形品は、次いで二次金型中に保持され、流体吹
き込み下に最終容器形状に成形される。Secondary Blow Molding The molded product, which has been cooled and has the predetermined panel-like recesses formed therein, is then held in a secondary mold and molded into the final container shape under fluid blowing.
この二次ブロー成形(最終吹込み成形)に際し
ては、最終容器形状に保持する様な成形乃至保形
が行なわれれば十分であり、成形品のどの部分に
ついても延伸の程度は可及的に低くするのがよ
い。二次金型の型内面温度は当然のことながら一
次金型の型内面温度よりも低いものであり、一般
に10乃至70℃の温度が適当である。 During this secondary blow molding (final blow molding), it is sufficient to perform molding or shape retention to maintain the final container shape, and the degree of stretching of any part of the molded product is kept as low as possible. It is better to do so. The inner surface temperature of the secondary mold is naturally lower than that of the primary mold, and generally a temperature of 10 to 70°C is appropriate.
かくして得られた延伸ポリエステルボトルは、
内容物を70乃至98℃の温度で熱間充填し、或いは
内容物を充填後、70乃至95℃の温度で加熱滅菌す
るための密封保存容器として有用である。 The stretched polyester bottle thus obtained is
It is useful as a sealed storage container for hot filling the contents at a temperature of 70 to 98°C, or for heating sterilization at a temperature of 70 to 95°C after filling.
以上、本発明の製造法を所謂ツーモールド法に
よる熱固定延伸ポリエステルボトルの製造に適用
した場合を例にとつて説明したが、かかる本発明
はこれに限定されるものではなく、例えば延伸ブ
ロー成形を行なう金型を熱処理すべき高温に維持
し、延伸ブロー成形に続いてこの金型内で熱処理
を行ない、更に金型内で冷却して取出す所謂ワ
ン・モールド法にも適用し得ることは、当業者で
あれば容易に理解されよう。 The manufacturing method of the present invention has been described above using an example in which the manufacturing method of the present invention is applied to the manufacture of a heat-set stretched polyester bottle by the so-called two-mold method, but the present invention is not limited to this. For example, stretch blow molding The fact that it can also be applied to the so-called one-mold method, in which a mold for carrying out the process is maintained at a high temperature for heat treatment, heat treatment is performed in this mold following stretch blow molding, and then the mold is cooled in the mold and taken out. It will be easily understood by those skilled in the art.
(発明の効果)
本発明の製造法によれば、ボトルの胴部に形成
されるパネル状凹部の肉厚を他の部分に比して薄
肉とすることができ、この結果としてパネル状凹
部は容器内圧の変化に応じて容易に変形するた
め、熱間充填や加熱殺菌により容器がみにくく変
形して外観特性が損われるという不都合が有効に
防止される。(Effects of the Invention) According to the manufacturing method of the present invention, the wall thickness of the panel-shaped recess formed in the body of the bottle can be made thinner than other parts, and as a result, the panel-shaped recess is Since the container easily deforms in response to changes in the internal pressure of the container, it is effectively possible to prevent the container from becoming unsightly and deformed due to hot filling or heat sterilization, thereby impairing its appearance characteristics.
第1図は、本発明の製造方法によつて得られる
ボトルの一例を示す図、第2−A図及び第2−B
図は、本発明の製造方法において、延伸ブロー成
形によつて得られる成形構造物の胴部における凸
部の状態を示す図、第3図は、上記凸部を反転さ
せて凹部とする手段の一例を示す図である。
3……パネル状凹部、4……柱部、10……金
型、20……凸部。
FIG. 1 is a diagram showing an example of a bottle obtained by the manufacturing method of the present invention, FIG. 2-A, and FIG. 2-B.
The figure shows the state of a convex part in the body of a molded structure obtained by stretch blow molding in the manufacturing method of the present invention, and FIG. 3 shows the means for inverting the convex part to form a concave part. It is a figure showing an example. 3...Panel-shaped recessed part, 4...Column part, 10...Mold, 20...Protrusion part.
Claims (1)
口頚部に対応する首部を有する有底プリフオーム
を、ブロー金型内にて二軸延伸ブロー成形し、相
対的に径の大きい凸部が所定間隔で胴部に形成さ
れている形状の中間成形品を製造し、次いでこの
中間成形品の胴部に形成されている凸部を反転さ
せてパネル状凹部として最終容器形状とすること
を特徴とする二軸延伸ポリエステルボトルの製造
法。 2 ブロー金型内での二軸延伸ブロー成形に際
し、該ブロー金型を熱固定温度に加熱し、該金型
内で熱固定を行なう特許請求の範囲第1項記載の
製造法。[Claims] 1. A bottomed preform made of thermoplastic polyester and having a neck corresponding to the neck of a container is biaxially stretched and blow-molded in a blow mold to form a convex portion with a relatively large diameter. It is characterized by manufacturing an intermediate molded product having a shape formed on the body at predetermined intervals, and then inverting the protrusions formed on the body of this intermediate molded product to form panel-like recesses to form the final container shape. A method for manufacturing biaxially oriented polyester bottles. 2. The manufacturing method according to claim 1, wherein during biaxial stretch blow molding in a blow mold, the blow mold is heated to a heat setting temperature and heat set is performed within the mold.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62033358A JPS63202425A (en) | 1987-02-18 | 1987-02-18 | Manufacture of biaxially stretched polyester bottle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62033358A JPS63202425A (en) | 1987-02-18 | 1987-02-18 | Manufacture of biaxially stretched polyester bottle |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63202425A JPS63202425A (en) | 1988-08-22 |
| JPH0473696B2 true JPH0473696B2 (en) | 1992-11-24 |
Family
ID=12384359
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62033358A Granted JPS63202425A (en) | 1987-02-18 | 1987-02-18 | Manufacture of biaxially stretched polyester bottle |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63202425A (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5255889A (en) * | 1991-11-15 | 1993-10-26 | Continental Pet Technologies, Inc. | Modular wold |
| CA2425972C (en) | 2003-04-11 | 2010-06-01 | Wentworth Mold Inc. | Hot fill mold shell assembly with reduced heat transfer |
| US6948924B2 (en) | 2003-04-11 | 2005-09-27 | Wentworth Mold Inc. | Mold assembly with modular mold shells |
| US8070470B2 (en) | 2009-02-06 | 2011-12-06 | Wentworth Mold Ltd. | Mold assembly |
| CA3041588A1 (en) * | 2016-10-25 | 2018-05-03 | Alan Mark Crawley | Improvements in double-walled containers |
-
1987
- 1987-02-18 JP JP62033358A patent/JPS63202425A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63202425A (en) | 1988-08-22 |
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