JPS63216B2 - - Google Patents

Info

Publication number
JPS63216B2
JPS63216B2 JP53045117A JP4511778A JPS63216B2 JP S63216 B2 JPS63216 B2 JP S63216B2 JP 53045117 A JP53045117 A JP 53045117A JP 4511778 A JP4511778 A JP 4511778A JP S63216 B2 JPS63216 B2 JP S63216B2
Authority
JP
Japan
Prior art keywords
bottle
polyethylene terephthalate
temperature
terephthalate resin
intermediate material
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
Application number
JP53045117A
Other languages
Japanese (ja)
Other versions
JPS54137060A (en
Inventor
Yoshiaki Hayashi
Koichi Haraguchi
Yukio Koshidaka
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.)
Yoshino Kogyosho Co Ltd
Original Assignee
Yoshino Kogyosho 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 Yoshino Kogyosho Co Ltd filed Critical Yoshino Kogyosho Co Ltd
Priority to JP4511778A priority Critical patent/JPS54137060A/en
Publication of JPS54137060A publication Critical patent/JPS54137060A/en
Publication of JPS63216B2 publication Critical patent/JPS63216B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/08Biaxial stretching during blow-moulding
    • B29C49/10Biaxial stretching during blow-moulding using mechanical means for prestretching
    • B29C49/12Stretching rods
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/42Component parts, details or accessories; Auxiliary operations
    • B29C49/78Measuring, controlling or regulating
    • B29C49/786Temperature
    • B29C2049/7864Temperature of the mould
    • B29C2049/78645Temperature of the mould characterised by temperature values or ranges
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/42Component parts, details or accessories; Auxiliary operations
    • B29C49/58Blowing means

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Moulds For Moulding Plastics Or The Like (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、主として醤油や炭酸飲料等のように
低温〜常温充填によつて充填される充填物の用途
に供せられるポリエチレンテレフタレート樹脂製
壜の製造方法である。
[Detailed Description of the Invention] [Industrial Field of Application] The present invention relates to a polyethylene terephthalate resin bottle that is mainly used for filling materials such as soy sauce and carbonated beverages by low-temperature to normal temperature filling. This is a manufacturing method.

[従来の技術] 二軸延伸処理によつて二軸方向に配向させたポ
リエチレンテレフタレート樹脂製壜は、分子鎖が
配列され、微結晶が形成されて、機械的強度や耐
ガス透過性が向上しており、しかも透明性に優
れ、かつ、無毒性であるということから、液体調
味料の充填等の用途において広く利用され始めて
いる。
[Prior Art] A polyethylene terephthalate resin bottle that is biaxially oriented by biaxial stretching has molecular chains aligned and microcrystals formed, resulting in improved mechanical strength and gas permeability. Furthermore, because it has excellent transparency and is non-toxic, it has begun to be widely used in applications such as filling liquid seasonings.

[発明が解決しようとする問題点] ところで、前記二軸延伸処理により得られたポ
リエチレンテレフタレート樹脂製壜は、前述の二
軸延伸の結果、機械的強度や耐ガス透過性は向上
するものの、この二軸延伸によつて壜壁内部に著
しい歪みが残存することとなり、この歪みが、例
えば壜の成形後内填物の充填工程までの間のよう
な短時間内の経時においてさえも緩和されようと
する力を生ずるため、収縮を起すこととなり、か
かる収縮が壜成形の際の脱型時における冷却工程
で起る壜の収縮に加えて生ずることとなる。この
ため、前記二軸延伸処理に付されたポリエチレン
テレフタレート樹脂製壜は、たとえ、常温下にお
いてさえも寸法安定性において著しい難点を有し
ているのが実情である。
[Problems to be Solved by the Invention] Incidentally, although the polyethylene terephthalate resin bottle obtained by the biaxial stretching process has improved mechanical strength and gas permeability as a result of the biaxial stretching process, Due to biaxial stretching, significant distortion remains inside the bottle wall, and this distortion may be alleviated even over a short period of time, such as after the bottle is formed and before the filling process. This force causes shrinkage, and this shrinkage occurs in addition to the shrinkage of the bottle that occurs during the cooling process during demolding during bottle molding. For this reason, the polyethylene terephthalate resin bottle subjected to the biaxial stretching process has a significant problem in dimensional stability even at room temperature.

これに対して、本発明は、入目(容量)が正確
で、二軸延伸処理により付与される機械的強度を
そのまま具備し、しかも経時に伴なう変形度が極
めて小さく、かつ優れた透明性を具備するポリエ
チレンテレフタレート樹脂製壜を、効率良く、か
つ経済的に得る方法を提供するものである。
In contrast, the present invention has accurate grain (capacity), maintains the mechanical strength imparted by biaxial stretching, has extremely low deformation over time, and has excellent transparency. The purpose of the present invention is to provide a method for efficiently and economically obtaining a polyethylene terephthalate resin bottle having properties.

[問題点を解決するための手段] 本発明のポリエチレンテレフタレート樹脂製壜
の製造方法は、ポリエチレンテレフタレート樹脂
のガラス転移温度以上で、かつ、融点以下の延伸
温度に加熱させたポリエチレンテレフタレート樹
脂製の有底円筒状の中間素材を、吹込み成形用金
型内で二軸延伸,熱固定処理することによつて壜
を製造する際に、前記吹込み成形用金型のサイズ
を、成形後の壜の脱型時における冷却工程中に起
る壜の収縮量が加算された大きさとされているも
のを使用し、また、該吹込み成形金型の加熱温度
を、ポリエチレンテレフタレート樹脂のガラス転
移温度以上でしかも前記延伸温度と90℃とのいず
れの温度をを超えることのない温度とし、さら
に、前記延伸温度に加熱させたポリエチレンテレ
フタレート樹脂製の有底円筒状の中間素材を二軸
方向に膨張させるとともに前記中間素材の外壁面
を前記成形用金型の内壁面に少なくとも5秒間以
上密接させることからなる二軸延伸,熱固定処理
を行なうポリエチレンテレフタレート樹脂製壜の
製造方法である。
[Means for Solving the Problems] The method for producing a polyethylene terephthalate resin bottle of the present invention comprises a polyethylene terephthalate resin bottle heated to a stretching temperature above the glass transition temperature and below the melting point of the polyethylene terephthalate resin. When manufacturing a bottle by biaxially stretching and heat-setting a bottom cylindrical intermediate material in a blow-molding mold, the size of the blow-molding mold is set to the size of the bottle after molding. The size of the blow-molding mold is set to include the amount of shrinkage of the bottle that occurs during the cooling process during demolding, and the heating temperature of the blow-molding mold is set to be higher than the glass transition temperature of the polyethylene terephthalate resin. Moreover, the temperature is set so as not to exceed either the stretching temperature or 90° C., and the bottomed cylindrical intermediate material made of polyethylene terephthalate resin heated to the stretching temperature is expanded in biaxial directions. In addition, the method for producing a polyethylene terephthalate resin bottle includes biaxial stretching and heat setting, which comprises bringing the outer wall surface of the intermediate material into close contact with the inner wall surface of the molding die for at least 5 seconds.

以下図面を参照して本発明のポリエチレンテレ
フタレート樹脂製壜の製造方法を説明する。
The method for manufacturing a polyethylene terephthalate resin bottle of the present invention will be explained below with reference to the drawings.

本発明方法においては、好ましくは固有粘度が
少なくとも0.55以上のポリエチレンテレフタレー
ト樹脂を使用し、押出パリソンによる成形法ある
いは射出パリソンによる成形法等、任意の成形手
段で製作された先端に丸味のある有底円筒状の中
間素材1を利用する。この中間素材1の口頚部2
とキヤツプ螺合用のねじ3とは、目的とする壜の
口頚部およびねじとそれぞれ同一の形状に形成さ
れているものが便利である。
In the method of the present invention, preferably a polyethylene terephthalate resin having an intrinsic viscosity of at least 0.55 is used, and the resin has a rounded end and is manufactured by any molding method such as an extrusion parison molding method or an injection parison molding method. A cylindrical intermediate material 1 is used. Mouth and neck part 2 of this intermediate material 1
It is convenient that the screw 3 for screwing the cap and the cap are formed in the same shape as the neck and the screw of the intended bottle.

中間素材1の製作にあたつては、成形工程に続
く冷却を徐冷にすると、結晶の増大によつて所謂
白化現象を生じ、透明性の低下がおこるので、成
形温度から常温への冷却は急冷によつて行わなけ
ればならない。
When producing the intermediate material 1, cooling from the molding temperature to room temperature is not recommended, since if the cooling following the molding process is slow cooling, the so-called whitening phenomenon will occur due to the increase in crystals, resulting in a decrease in transparency. This must be done by rapid cooling.

本発明方法においては、製作されたポリエチレ
ンテレフタレート樹脂製の中間素材1を、吹込み
成形用金型内にセツトし、しかる後に二軸方向に
延伸させ、延伸工程の最終工程において中間素材
1の外壁面4を成形用金型の内壁面に少なくとも
5秒間以上密接させて熱固定を行なうものである
が、中間素材を吹込み成形用金型内にセツトさせ
て二軸方向に延伸処理するに当つては、中間素材
を、該中間素材を構成するポリエチレンテレフタ
レート樹脂のガラス転移温度以上,融点以下の延
伸温度に加熱させておくことと、および前記吹込
み成形用金型を同じくポリエチレンテレフタレー
ト樹脂のガラス転移温度以上で、かつ前述の延伸
温度と90℃とのいずれをも超えることのない熱固
定温度に加熱させておくことが必要である。
In the method of the present invention, the manufactured intermediate material 1 made of polyethylene terephthalate resin is set in a blow molding mold, and then stretched in biaxial directions, and in the final step of the stretching process, the intermediate material 1 is extruded. Heat fixing is carried out by bringing the wall surface 4 into close contact with the inner wall surface of the mold for at least 5 seconds. In this case, the intermediate material is heated to a stretching temperature that is higher than the glass transition temperature and lower than the melting point of the polyethylene terephthalate resin constituting the intermediate material, and the blow molding mold is heated to a stretching temperature that is lower than the melting point of the polyethylene terephthalate resin. It is necessary to heat the film to a heat-setting temperature that is above the transition temperature and does not exceed either the above-mentioned stretching temperature or 90°C.

したがつて、前述のポリエチレンテレフタレー
ト樹脂製の中間素材1を二軸延伸処理および熱固
定処理が施される吹込み成形用金型内にセツトす
る直前に、加熱室でポリエチレンテレフタレート
樹脂のガラス転移温度以上,融点以下の分子配向
可能な延伸温度、すなわち一般的には70〜220℃
に加熱しなければならない。
Therefore, immediately before setting the aforementioned intermediate material 1 made of polyethylene terephthalate resin into a blow molding mold where it is subjected to biaxial stretching treatment and heat setting treatment, the glass transition temperature of the polyethylene terephthalate resin is heated in a heating chamber. Stretching temperature that allows molecular orientation, which is below the melting point, that is, generally 70 to 220℃
must be heated to.

所定の温度に加熱した中間素材1を、第2図の
符号5で示すような吹込み成形用金型内にセツト
し、次いで、中間素材1内に圧縮空気を吹込み、
中間素材1を膨張させると同時に押下げ棒6で、
中間素材1の底部4を押下げ、第2図に示すよう
に、中間素材1の外壁面1aが成形用金型5の内
壁面5aに接触するまで二軸方向に延伸させ、し
かる後、膨張した中間素材1の外壁面1aを、所
定の温度に加熱されている成形用金型5の内壁面
5aに少なくとも5秒以上密接させて熱固定処理
を行い、所定の壜7形状を有する成形品を製作す
るものである。
The intermediate material 1 heated to a predetermined temperature is set in a blow molding mold as shown by the reference numeral 5 in FIG. 2, and then compressed air is blown into the intermediate material 1.
At the same time as expanding the intermediate material 1, using the push-down rod 6,
The bottom part 4 of the intermediate material 1 is pushed down, and as shown in FIG. The outer wall surface 1a of the intermediate material 1 is brought into close contact with the inner wall surface 5a of the molding die 5 heated to a predetermined temperature for at least 5 seconds to perform a heat setting process, thereby producing a molded product having a predetermined bottle shape. It is intended to produce.

前記図面に示される延伸処理工程は、押下げ棒
6の軸線上に圧縮空気孔8を穿設し、その下端お
よび側面に吹出し口91,92,93を設けておく
ことにより、押下げ棒6を膨張用の圧縮空気送入
口として利用する場合を示しているものである
が、二軸延伸処理は、前記した通り、成形用金型
5内にセツトした中間素材1を同時二軸延伸によ
つて膨張させる方法でも、あるいは圧縮空気を吹
き込んで中間素材1を膨張させるに先立つて予め
押下げ棒6のみを作動させて中間素材1を軸心方
向のみの一軸方向に延伸し、次いで圧縮空気を吹
込んで軸心方向に延伸されている中間素材1を更
に半径方向に延伸する逐次二軸延伸法による方法
でも良い。
The stretching process shown in the drawings is performed by drilling a compressed air hole 8 on the axis of the push-down rod 6 and providing blow-off ports 9 1 , 9 2 , 9 3 on the lower end and side surface of the push-down rod 6 . This shows a case where the lowering rod 6 is used as a compressed air inlet for expansion, but the biaxial stretching process is performed by simultaneously biaxially stretching the intermediate material 1 set in the molding die 5, as described above. Alternatively, before expanding the intermediate material 1 by blowing compressed air, only the push-down rod 6 is actuated to stretch the intermediate material 1 uniaxially only in the axial direction, and then A sequential biaxial stretching method may also be used, in which the intermediate material 1, which has been stretched in the axial direction, is further stretched in the radial direction by blowing compressed air.

本発明方法における二軸延伸処理後の熱固定処
理は、熱固定処理に先立つて行われる延伸処理に
よつて膨張している中間素材1の外壁面1aを成
形用金型5の内壁面5aに密接させて行うもので
あるが、この熱固定処理時の金型の温度が延伸温
度を超えるような高温に加熱されていると所謂白
化現象が生じ失透の原因となり、また、90℃を超
えるような場合は、この熱処理工程のための加熱
制御が複雑となるばかりでなく、熱処理のために
かかる経費が高騰して不経済となるものでもある
から、前記熱固定処理時の金型の温度は、延伸温
度以下でかつ90℃以下とされていなければならな
い。他方、前記熱固定処理時の金型の温度が、前
記中間素材1を構成しているポリエチレンテレフ
タレート樹脂のガラス転移温度に達しないような
低温の場合には、歪みの除去という熱固定処理の
目的を十分に達成させることができないから、熱
固定処理時における成形用金型はポリエチレンテ
レフタレート樹脂のガラス転移温度以上とされて
いなければならないものである。
In the heat setting process after the biaxial stretching process in the method of the present invention, the outer wall surface 1a of the intermediate material 1, which has expanded due to the stretching process performed prior to the heat setting process, is fixed to the inner wall surface 5a of the molding die 5. However, if the temperature of the mold during this heat setting treatment is heated to a high temperature that exceeds the stretching temperature, a so-called whitening phenomenon will occur and cause devitrification. In such a case, not only is the heating control for this heat treatment process complicated, but the cost for heat treatment rises and becomes uneconomical. must be below the stretching temperature and below 90°C. On the other hand, if the temperature of the mold during the heat setting process is low enough to not reach the glass transition temperature of the polyethylene terephthalate resin constituting the intermediate material 1, the purpose of the heat setting process is to remove distortion. Since this cannot be achieved satisfactorily, the mold used for heat setting must have a temperature higher than the glass transition temperature of the polyethylene terephthalate resin.

更に、前記温度での熱固定処理によつて所望の
寸法安定性を得るためには、膨張している中間素
材1の外壁面1aを成形用金型5の内壁面5aに
少なくとも5秒間以上密接させることが必要であ
り、密接時間を5秒未満の瞬時にすると十分な歪
みの除去を行なうことができない。
Furthermore, in order to obtain the desired dimensional stability through the heat setting treatment at the above temperature, the outer wall surface 1a of the expanding intermediate material 1 is brought into close contact with the inner wall surface 5a of the molding die 5 for at least 5 seconds. If the contact time is less than 5 seconds, sufficient distortion cannot be removed.

熱固定処理の完了後は直ちに壜7の温度を適宜
な方法で降下させ、取り出し時における壜7の変
形を防止したうえで成形用金型5から壜7を取り
出すのが良い。
Immediately after the heat setting process is completed, it is preferable to lower the temperature of the bottle 7 by an appropriate method to prevent the bottle 7 from being deformed during removal, and then take the bottle 7 out of the molding die 5.

なお、吹込み成形用金型5の加熱,冷却は、例
えば成形用金型5中に熱源と冷却用液体等を通過
させる透孔とを同時に設けておき、所定の熱固定
温度への加熱は冷却用液体の流通を停止して熱源
をセツトすることにより、また熱固定処理後の冷
却は熱源をオフにして冷却用液体を流通させるこ
とによつて行なうことができ、したがつて熱固定
処理された壜7の冷却は成形用金型5を冷却する
ことによつても、あるいは成形用金型5にセツト
されている壜7内に直接冷却空気を吹き込むこと
によつてもできる。
The blow molding mold 5 can be heated and cooled by, for example, simultaneously providing a heat source and a through hole through which a cooling liquid or the like passes through the molding mold 5, and heating to a predetermined heat fixing temperature. By stopping the flow of the cooling liquid and setting the heat source, cooling after the heat setting process can be performed by turning off the heat source and allowing the cooling liquid to flow, so that the heat setting process The bottle 7 can be cooled by cooling the mold 5 or by directly blowing cooling air into the bottle 7 set in the mold 5.

更に、前述の通りの延伸,熱固定処理を終えて
吹込み成形用金型から壜を脱型する際の冷却時に
は、熱固定温度および時間に応じて相当量の収縮
が起り、入目(容量)が金型から計算されるもの
とは異なつてくるので、本発明方法においてはか
かる収縮量を見越した大きさの吹込み成形用金型
を使用することが必要である。なお、延伸、熱固
定処理を終えて、吹込み成形用金型から脱型する
際の冷却時における成形された壜の収縮量は、一
般に熱固定温度が高い程、また熱固定時間が短い
程大きく、因みに熱固定時間8秒で、温度70℃の
場合には約4.3%程度、80℃の場合には約4.6%程
度、90℃の場合には約5.3%程度の収縮が起るこ
とが確認されているので、熱固定時間および熱固
定温度に応じて変化する収縮量を相殺し得る大き
さにされている吹込み成形用金型を使用すること
が必要である。
Furthermore, during the cooling process when removing the bottle from the blow-molding mold after completing the stretching and heat-setting treatments as described above, a considerable amount of shrinkage occurs depending on the heat-setting temperature and time. ) will be different from that calculated from the mold, so in the method of the present invention it is necessary to use a blow molding mold of a size that takes into account such shrinkage. In general, the higher the heat-setting temperature and the shorter the heat-setting time, the smaller the amount of shrinkage of the molded bottle during cooling when it is removed from the blow-molding mold after stretching and heat-setting. By the way, when the heat setting time is 8 seconds, the shrinkage will be about 4.3% at 70℃, about 4.6% at 80℃, and about 5.3% at 90℃. As has been established, it is necessary to use blow molds that are sized to compensate for the amount of shrinkage that varies with heat setting time and heat setting temperature.

[実施例] 射出パリソン方式によりポリエチレンテレフタ
レート樹脂製の中間素材を作製し、これを延伸温
度たる95℃に加熱してから、86℃の熱固定温度に
加熱されている全高255mm,容量1の壜吹込み
成形用金型内にセツトし、しかる後に圧縮空気を
吹込み、blowing時間6秒間,8秒間,10秒間の
それぞれ3種類の二軸延伸、熱固定されたポリエ
チレンテレフタレート樹脂製の透明性に優れた壜
を成形した。
[Example] A bottle with a total height of 255 mm and a capacity of 1 is produced by producing an intermediate material made of polyethylene terephthalate resin by the injection parison method, heating it to the stretching temperature of 95 °C, and then heating it to the heat setting temperature of 86 °C. It is set in a blow molding mold, and then compressed air is blown into the transparent polyethylene terephthalate resin that has been biaxially stretched and heat-set in three different ways with blowing times of 6 seconds, 8 seconds, and 10 seconds. Made an excellent bottle.

なお、本方法においては、中間素材の外壁を金
型の内壁に密接させる熱固定時間は、殆ど
blowing時間と同一であると見做し得るものであ
る。
In addition, in this method, the heat setting time for bringing the outer wall of the intermediate material into close contact with the inner wall of the mold is almost
This can be considered to be the same as the blowing time.

得られた3種類の壜の成形30分後における全高
および入目を第3図に示す。
Figure 3 shows the total height and opening of the three types of bottles obtained after 30 minutes of molding.

得られた3種類の成形30分後における壜に70℃
の温水を充填し、常温に2時間放置したあとで測
定した壜の全高および入目の変化量を、温水充填
前の壜の全高および入目との差で第4図に示す。
The resulting three types of bottles were heated to 70°C after 30 minutes of molding.
Fig. 4 shows the changes in the total height and opening of the bottle measured after filling with warm water and leaving it at room temperature for 2 hours, and the difference from the total height and opening of the bottle before filling with hot water.

同じく得られた3種類の成形30分後における壜
をさらに40℃,RH75%のオーブン中に1〜5日
間放置したあとで測定した壜の全高および入目の
経時変化量を、オーブン中に放置する前の壜の全
高および入目との差で第5図に示す。
The three types of bottles obtained in the same manner after 30 minutes of molding were further left in an oven at 40℃ and RH75% for 1 to 5 days, and the changes in the total height and mesh of the bottles over time were measured. Figure 5 shows the total height of the bottle before filling and the difference between the opening and opening.

第4図より、本発明方法によつて得られた二軸
延伸,熱固定されたポリエチレンテレフタレート
樹脂製の壜は、70℃の高温液体の充填に十分耐え
る高温寸法安定性に優れた性質を具備するもので
あることが明らかであり、更に第5図より、経時
変化に伴なう変化量が小さい寸法安定性に優れた
性質を具備するものであることが明らかである。
From Figure 4, the biaxially stretched and heat-set polyethylene terephthalate resin bottle obtained by the method of the present invention has excellent high-temperature dimensional stability that can withstand filling with high-temperature liquid at 70°C. Furthermore, from FIG. 5, it is clear that the material has excellent dimensional stability with a small amount of change over time.

[発明の作用および効果] 本発明のポリエチレンテレフタレート樹脂製壜
の製造方法は、有底円筒状の中間素材を該中間素
材を構成するポリエチレンテレフタレート樹脂の
ガラス転移温度以上,融点以下の延伸温度による
二軸延伸処理に付した結果生成する壜壁内部の著
しい歪みを、前記二軸延伸処理に引き続いて直ち
に、膨張状態にある中間素材の外壁を、ポリエチ
レンテレフタレート樹脂のガラス転移温度以上
で、かつ、前記延伸温度以下で、しかも90℃以下
の温度に予め加熱されている吹込み成形用金型の
内壁に少なくとも5秒間以上密接させる熱固定処
理を行なうことによつて除去するもので、二軸延
伸処理により付与される機械的強度をそのまま具
備し、しかも経時に伴なう変形度が極めて小さ
く、かつ優れた透明性を具備するポリエチレンテ
レフタレート樹脂製の壜が確実に得られるという
作用、効果を奏するものである。
[Operations and Effects of the Invention] The method for producing a polyethylene terephthalate resin bottle of the present invention comprises stretching a bottomed cylindrical intermediate material at a stretching temperature of at least the glass transition temperature and below the melting point of the polyethylene terephthalate resin constituting the intermediate material. Immediately following the biaxial stretching process, the outer wall of the intermediate material in the expanded state is heated to a temperature higher than the glass transition temperature of the polyethylene terephthalate resin, and the inner wall of the bottle is subjected to the axial stretching process. It is removed by heat-setting the inner wall of a blow-molding mold, which has been heated in advance to a temperature below the stretching temperature and below 90°C, for at least 5 seconds. A bottle made of polyethylene terephthalate resin that retains the same mechanical strength as it is, has extremely low deformation over time, and has excellent transparency. It is.

また本発明方法においては、前記膨張状態にあ
る中間素材の外壁を密接させる前記吹込み成形用
金型の大きさを、壜成形の際の脱型時における冷
却工程で起る壜の収縮量を相殺する大きさにして
いるので、入目の正確な壜が得られるという作
用,効果を奏するものである。
In addition, in the method of the present invention, the size of the blow molding mold that brings the outer wall of the expanded intermediate material into close contact with each other is adjusted to the amount of shrinkage of the bottle that occurs during the cooling process during demolding during bottle molding. Since the sizes are set to offset each other, it has the effect of making it possible to obtain a bottle with an accurate grain size.

更に本発明方法においては、壜成形の延伸工程
と熱固定工程とを同時に完了させる、すなわち、
延伸、熱固定処理されたポリエチレンテレフタレ
ート樹脂製壜の製造を一連の工程で完了させるも
のであるから、熱の利用効率が高く、しかも吹込
み成形用金型の加熱温度が90℃以下であるから金
型の加熱制御が容易で、かつ、加熱のための経費
も少なくて済む等の作用,効果を奏するものであ
る。
Furthermore, in the method of the present invention, the stretching step and heat setting step of bottle forming are completed simultaneously, that is,
Since the production of stretched and heat-set polyethylene terephthalate resin bottles is completed in a series of steps, heat utilization efficiency is high, and the heating temperature of the blow molding mold is 90℃ or less. This provides functions and effects such as easy heating control of the mold and less expense for heating.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明で利用する中間素材の1例を示
す断面図、第2図はその中間素材を金型にセツト
して壜に成形した状態を示す断面図、第3図は本
発明の一実施例によつて成形された壜の成形30分
後における全高、および入目(容量)を熱固定時
間の変化とともに示したグラフであり、第4図は
温水充填前後における壜の全高および入目(容
量)の変化量を熱固定時間の変化とともに示した
グラフであり、第5図は40℃,RH75%の雰囲気
中に放置前後の壜の全高および入目(容量)の変
化量を熱固定時間の変化とともに示したグラフで
ある。 1:中間素材、5:吹込み成形用金型、7:
壜、5a:成形用金型5の内壁面。
Fig. 1 is a sectional view showing an example of the intermediate material used in the present invention, Fig. 2 is a sectional view showing the intermediate material set in a mold and formed into a bottle, and Fig. 3 is a sectional view showing an example of the intermediate material used in the present invention. FIG. 4 is a graph showing the total height and filling (capacity) of a bottle molded according to one example after 30 minutes of molding, along with changes in heat setting time. This is a graph showing the amount of change in the size (capacity) along with the change in heat setting time. It is a graph shown along with changes in fixation time. 1: Intermediate material, 5: Blow mold, 7:
Bottle, 5a: Inner wall surface of molding die 5.

Claims (1)

【特許請求の範囲】[Claims] 1 ポリエチレンテレフタレート樹脂のガラス転
移温度以上で、かつ、融点以下の延伸温度に加熱
させたポリエチレンテレフタレート樹脂製の有底
円筒状の中間素材を、吹込み成形用金型内で二軸
延伸、熱固定処理することによつて壜を製造する
方法において、吹込み成形用金型の大きさが、成
形後の壜の脱型時における冷却工程中に起る壜の
収縮量が加算された大きさとされており、かつポ
リエチレンテレフタレート樹脂のガラス転移温度
以上でしかも前記延伸温度と90℃とのいずれの温
度をも超えることのない金型温度とされている吹
込み成形用金型内で、前記延伸温度に加熱されて
いるポリエチレンテレフタレート樹脂製の有底円
筒状の中間素材を二軸方向に膨張させ、前記中間
素材の外壁面を前記成形用金型の内壁面に少なく
とも5秒間以上密接させることにより、二軸延
伸、熱固定処理を行なうことを特徴とするポリエ
チレンテレフタレート樹脂製壜の製造方法。
1 A bottomed cylindrical intermediate material made of polyethylene terephthalate resin heated to a stretching temperature above the glass transition temperature and below the melting point of the polyethylene terephthalate resin is biaxially stretched and heat-set in a blow molding mold. In the method of manufacturing bottles by processing, the size of the blow molding mold is determined by adding the amount of shrinkage of the bottle that occurs during the cooling process when demolding the bottle after molding. In a blow mold, the stretching temperature is set at a temperature that is higher than the glass transition temperature of the polyethylene terephthalate resin and does not exceed either the stretching temperature or 90°C. By biaxially expanding a bottomed cylindrical intermediate material made of polyethylene terephthalate resin heated to , and bringing the outer wall surface of the intermediate material into close contact with the inner wall surface of the molding die for at least 5 seconds, A method for producing a polyethylene terephthalate resin bottle, which comprises performing biaxial stretching and heat setting.
JP4511778A 1978-04-17 1978-04-17 Production of saturated polyester bottle Granted JPS54137060A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4511778A JPS54137060A (en) 1978-04-17 1978-04-17 Production of saturated polyester bottle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4511778A JPS54137060A (en) 1978-04-17 1978-04-17 Production of saturated polyester bottle

Publications (2)

Publication Number Publication Date
JPS54137060A JPS54137060A (en) 1979-10-24
JPS63216B2 true JPS63216B2 (en) 1988-01-06

Family

ID=12710315

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4511778A Granted JPS54137060A (en) 1978-04-17 1978-04-17 Production of saturated polyester bottle

Country Status (1)

Country Link
JP (1) JPS54137060A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4482518A (en) * 1981-10-02 1984-11-13 Owens-Illinois, Inc. Methods for reducing post-mold shrinkage of hollow oriented polyethylene terephthalate containers

Family Cites Families (2)

* Cited by examiner, † Cited by third party
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
JPS53264A (en) * 1976-06-25 1978-01-05 Teijin Ltd Bottle made of polyester and method of producing same

Also Published As

Publication number Publication date
JPS54137060A (en) 1979-10-24

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