JPH058087B2 - - Google Patents
Info
- Publication number
- JPH058087B2 JPH058087B2 JP60215671A JP21567185A JPH058087B2 JP H058087 B2 JPH058087 B2 JP H058087B2 JP 60215671 A JP60215671 A JP 60215671A JP 21567185 A JP21567185 A JP 21567185A JP H058087 B2 JPH058087 B2 JP H058087B2
- Authority
- JP
- Japan
- Prior art keywords
- bottle
- parison
- mold
- temperature
- stretching
- 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
- B29C49/42—Component parts, details or accessories; Auxiliary operations
- B29C49/78—Measuring, controlling or regulating
- B29C49/786—Temperature
- B29C2049/7861—Temperature of the preform
- B29C2049/7862—Temperature of the preform characterised by temperature values or ranges
-
- 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
- B29C49/42—Component parts, details or accessories; Auxiliary operations
- B29C49/78—Measuring, controlling or regulating
- B29C49/786—Temperature
- B29C2049/7864—Temperature of the mould
- B29C2049/78645—Temperature of the mould characterised by temperature values or ranges
-
- 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
- B29C2949/00—Indexing scheme relating to blow-moulding
- B29C2949/07—Preforms or parisons characterised by their configuration
- B29C2949/0715—Preforms or parisons characterised by their configuration the preform having one end closed
-
- 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
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2067/00—Use of polyesters or derivatives thereof, as moulding material
Landscapes
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
Description
(産業上の利用分野)
本発明は、エチレンテレフタレート系ポリエス
テル樹脂から、熱収縮が小さく、金型に忠実な形
状の二軸配向ボルトを高能率で得る方法に関する
ものである。
(従来技術)
ポリエチレンテレフタレートに代表されるポリ
エステル樹脂製のボトルは、透明性、強度、衛生
性等に優れているので、各種用途に多用されてい
るが、高温に晒されると熱収縮を起こすという難
点がある。
そこでその欠点を改良するため、ブロー延伸成
形したボルトを高温で熱処理する方法が知られて
いるが、かなり長時間熱処理しないと取出し時に
ボルトが収縮変形するため、ボルトの製造速度が
極めて遅くなつてしまう。
(発明が解決しようとする問題点)
本発明は、熱収縮性の小さいボトルを得ようと
すると製造速度が低下し、製造速度を向上させる
と熱収縮性の大きいボトルしか得られないという
従来の問題点を解決したものである。
(問題点を解決するための手段)
すなわち本発明は、ポリエステルの有底筒状パ
リソンを加熱して110〜125℃とし、そのパリソン
を、表面が80〜110℃に維持された金型内におい
て、25000%/分以上の延伸速度で延伸し、得ら
れたボトルを引き続き前記金型に押圧しつつ保持
した後、金型から離型することを特徴とするもの
である。
以下本発明を具体的に説明する。
本発明に使用するポリエステル樹脂は、エチレ
ンテレフタレート単位を70%以上含むものであつ
て、極限粘度0.6以上の通常の樹脂を用いること
ができる。
このポリエステル樹脂からパリソンを得る方法
も従来より周知のもので、射出成形により有底筒
状のパリソンを得るか、あるいは押出成形により
製造したパイプの一端を閉じて有底筒状にする方
法による。
このパリソンを延伸ブロー成形するにあたつて
は、パリソン温度を110〜125℃の範囲とし、表面
が80〜110℃に維持された金型内で、25000%/分
以上の延伸速度でブロー延伸を行うことが重要で
ある。
一般に金型温度を高くすると、ブロー延伸成形
されたボトルが金型と接触したときの熱処理効果
が大きく、ボトルの熱収縮性は小さくなるが、
100℃を越えるような高温では、ボトルを金型か
らとりだす時にボトルが収縮変形してしまい、短
時間では所定の形状、容量のボトルが得られな
い。
そこで検討の結果、金型温度を80〜100℃の範
囲とすると、ボトルを金型と短時間接触させるだ
けでかなりの熱収縮性低減効果があり、ボトルの
取出しも可能なことが判明したが、ボトルの収縮
変形が未だ残り、十分とはいえなかつた。
そこでさらに検討の結果、パリソン温度を通常
の温度よりも高い110〜125℃まで上げてブロー延
伸すると、金型温度を110℃程度まで上げてもボ
トルを金型形状に忠実なままで取出することがで
きて熱収縮も小さくなること、反面ボトルの強度
はやや低下するが、これは延伸速度を25000%以
上という高速延伸とすることにより解決し得るこ
とを見い出したのである。
パリソン温度が110℃よりも低いと、80〜110℃
に維持した金型を用いた場合取出したボトルの形
状が正確に出ず、また125℃よりも高いと、加熱
中にパリソンに救晶白化が生じやすい。
ポリエステル樹脂のパリソンを内外面同等に
110〜125℃に加熱するには、パリソンを内外両面
から加熱するのが好ましい。外面のみから加熱し
た場合には、延伸倍率が最も大きくなるパリソン
の内面が低温となつて、所望のボトルを得るのは
困難である。
パリソンを内面から加熱する方法としては、
(1) パリソン内部に示外線ヒータ等の輻射ヒータ
を挿入する方法
(2) パリソン内部に熱風吹出しロツドを挿入し、
熱風加熱する方法。
(3) パリソン内部に黒体ロツドを挿入し、外部の
赤外線ヒータよりの輻射線のうち、ポリエステ
ルのパリソンにより吸収されない可視ないし近
赤外域の光線を内部のロツドに吸収させて昇温
させる方法
等がある。
また内面に軸方向の温度分布を付けたい場合に
は、パリソンの長さよりも大幅に短い幅射ヒータ
をパリソン軸方向に所定の移動一停止パターンで
動かして、パリソンの部分毎にヒータによる加熱
時間をかえて所望の温度プロフアイルを付与する
方法も有効である。
金型は、その表面を80〜110℃に維持する。80
℃よりも低いとボトルの熱収縮性が大きくなり、
110℃を越えるとボトル取出し時の収縮変形が大
きくなる。
延伸速度は、25000%/分以上、好ましくは
35000%/分以上に設定する。
それ以下では、パリソンが高温のため延伸配向
効果が小さくなり、ボトルの強度が低下すること
になる。延伸速度の上限は、50000%/分程度で
ある。
延伸速度は、ブロー用エアの吹き込み量等で調
整することができる。なおここで延伸速度とは、
周方向の延伸倍率(%で表示、例えば倍率3倍は
200%)を、ブロー延伸開始から金型に接触する
までの時間で割つた周方向の平均延伸速度であ
る。軸方向の延伸速度は、通常軸方向倍率が周方
向倍率よりも小さいことにより、これよりも小さ
くなるのが普通である。
延伸倍率は、ボトルに十分な強度を付与するた
め、それ自体普通の条件である軸方向2〜3倍、
周方向3〜4倍の範囲内で、できるだけ高い倍率
にするがよい。
ブロー延伸成形されたボトルは、内圧(ブロー
圧)を維持したまま金型内面と2〜15秒程度接触
させた後内圧を解除して、特に冷却工程を置くこ
となくそのまま取出せる。
(実施例)
極限粘度0.85のポリエチレンテレフタレート樹
脂から、射出成形により、胴部外径27mm、長さ
125mm、厚さ3.6mmのパリソンを製造した。これを
赤外線ヒータにより内外面から加熱した後ブロー
延伸成形し、内圧を保持したまま金型と4秒間接
触させてから取出して、胴部外径83mm、高さ275
mm、容量1リツトルのボトルとした。延伸倍率
は、軸方向2.5倍、周方向3.5倍となる。
ここで、パリソン温度、金型温度、および延伸
速度をかえて、得られたボトルについて次の品質
項目を評価した。
(1) 熱収縮率
室温で満注容量を測定したボトルに、72℃の
温水を首部下端まで入れ、無栓のまま24時間室
温で放置した後その満注容量も測定し、容量の
減少率を%で表示した。
(2) 引張り降伏強度
ボトルの周方向に沿つて採取した長さ65mm、
幅3mmのテストピースをASTM−D1822に準
じて引張の速度50mm/分で引張つたときの降伏
点強度をもとめた。
(3) ボトル形状
金型より取出し直後のボトルの収縮率が、金
型形状と比較して、容量で5%以下、寸法で2
%以下のものを〇、それよりも大きいものを×
とした。
ブロー延伸成形条件およびボトルの品質評価結
果を第1表に併せて示す。
(Industrial Application Field) The present invention relates to a highly efficient method for obtaining biaxially oriented bolts from ethylene terephthalate-based polyester resin that have low thermal shrinkage and have a shape that is faithful to the shape of a mold. (Prior art) Bottles made of polyester resin, typified by polyethylene terephthalate, are widely used for various purposes due to their excellent transparency, strength, and hygienic properties. However, they have been known to shrink when exposed to high temperatures. There are some difficulties. In order to overcome this drawback, a method is known in which blow-stretched bolts are heat treated at high temperatures, but if the bolts are not heat-treated for a considerable period of time, the bolts will shrink and deform when taken out, resulting in extremely slow bolt manufacturing speed. Put it away. (Problems to be Solved by the Invention) The present invention solves the conventional problem that trying to obtain a bottle with low heat shrinkability reduces the manufacturing speed, and increasing the manufacturing speed only results in a bottle with high heat shrinkability. This solves the problem. (Means for Solving the Problems) That is, the present invention heats a polyester cylindrical parison with a bottom to 110 to 125°C, and places the parison in a mold whose surface is maintained at 80 to 110°C. The bottle is stretched at a stretching speed of 25,000%/min or more, and the resulting bottle is subsequently held in the mold while being pressed, and then released from the mold. The present invention will be specifically explained below. The polyester resin used in the present invention contains 70% or more of ethylene terephthalate units, and a conventional resin having an intrinsic viscosity of 0.6 or more can be used. Methods for obtaining a parison from this polyester resin are also conventionally well known, such as obtaining a parison in the shape of a cylinder with a bottom by injection molding, or by closing one end of a pipe produced by extrusion molding to form a cylinder in the form of a cylinder with a bottom. In stretch-blow molding this parison, the parison temperature is in the range of 110 to 125°C, and the parison is blow-stretched at a stretching speed of 25,000%/min or more in a mold whose surface is maintained at 80 to 110°C. It is important to do this. In general, when the mold temperature is raised, the heat treatment effect when the blow stretch-molded bottle comes into contact with the mold becomes larger, and the heat shrinkability of the bottle becomes smaller.
At high temperatures exceeding 100°C, the bottle shrinks and deforms when it is removed from the mold, making it impossible to obtain a bottle with the desired shape and capacity in a short period of time. As a result of the study, it was found that when the mold temperature is set in the range of 80 to 100℃, it is possible to significantly reduce heat shrinkage by simply bringing the bottle into contact with the mold for a short time, and it is also possible to remove the bottle. However, the shrinkage and deformation of the bottle still remained, which could not be said to be sufficient. As a result of further investigation, we found that if we raise the parison temperature to 110-125℃, which is higher than normal temperature, and blow-stretch it, the bottle can be taken out while maintaining its mold shape even if the mold temperature is raised to about 110℃. They found that the strength of the bottle was slightly reduced, but this could be solved by stretching at a high speed of 25,000% or higher. When the parison temperature is lower than 110℃, 80~110℃
If a mold maintained at a constant temperature is used, the shape of the bottle taken out will not be accurate, and if the temperature is higher than 125°C, crystal whitening will likely occur in the parison during heating. Polyester resin parison on the inside and outside
To heat the parison to 110-125°C, it is preferable to heat the parison from both the inside and outside. If heating is performed only from the outer surface, the inner surface of the parison, where the stretching ratio is greatest, will be at a low temperature, making it difficult to obtain the desired bottle. Methods of heating the parison from the inside include (1) inserting a radiant heater such as an indicative heater inside the parison; (2) inserting a hot air blowing rod inside the parison;
How to heat with hot air. (3) A method in which a black body rod is inserted inside the parison, and among the radiation from an external infrared heater, visible to near-infrared light that is not absorbed by the polyester parison is absorbed by the internal rod to raise the temperature. There is. In addition, if you want to create an axial temperature distribution on the inner surface, you can move a radiation heater, which is much shorter than the length of the parison, in the axial direction of the parison in a predetermined movement-stop pattern, and heat each part of the parison over a heating time. It is also effective to provide a desired temperature profile by changing the temperature. The mold maintains its surface at 80-110℃. 80
If the temperature is lower than ℃, the heat shrinkage of the bottle will increase.
If the temperature exceeds 110℃, the shrinkage deformation when taking out the bottle will increase. The stretching speed is 25000%/min or more, preferably
Set to 35000%/min or higher. If the temperature is lower than that, the parison will be at a high temperature, so the stretching orientation effect will be reduced, and the strength of the bottle will be reduced. The upper limit of the stretching speed is about 50000%/min. The stretching speed can be adjusted by adjusting the amount of blowing air. Note that the stretching speed here is
Stretching magnification in the circumferential direction (displayed in %, for example, 3x magnification is
200%) divided by the time from the start of blow stretching to contact with the mold, which is the average stretching speed in the circumferential direction. The stretching speed in the axial direction is usually lower than this because the axial magnification is usually smaller than the circumferential magnification. The stretching ratio is 2 to 3 times in the axial direction, which is a normal condition, in order to give the bottle sufficient strength.
The magnification should be as high as possible within the range of 3 to 4 times in the circumferential direction. The blow-stretched bottle is brought into contact with the inner surface of the mold for about 2 to 15 seconds while maintaining the internal pressure (blow pressure), and then the internal pressure is released and the bottle can be taken out without any particular cooling process. (Example) By injection molding from polyethylene terephthalate resin with an intrinsic viscosity of 0.85, the body has an outer diameter of 27 mm and a length of
A parison of 125 mm and 3.6 mm thickness was manufactured. This was heated from the inside and outside with an infrared heater, then blow-stretched, and brought into contact with the mold for 4 seconds while maintaining the internal pressure, and then taken out.
mm, and the bottle had a capacity of 1 liter. The stretching ratio is 2.5 times in the axial direction and 3.5 times in the circumferential direction. Here, the following quality items were evaluated for the resulting bottles by changing the parison temperature, mold temperature, and stretching speed. (1) Heat shrinkage rate Fill a bottle with 72°C hot water up to the bottom of the neck, measure the full capacity at room temperature, leave it unstopped at room temperature for 24 hours, then measure the full capacity, and calculate the rate of decrease in capacity. is expressed as a percentage. (2) Tensile yield strength 65mm length taken along the circumferential direction of the bottle,
The yield point strength was determined when a test piece with a width of 3 mm was pulled at a tensile speed of 50 mm/min in accordance with ASTM-D1822. (3) Bottle shape The shrinkage rate of the bottle immediately after being removed from the mold is 5% or less in terms of capacity and 2% in dimensions compared to the shape of the mold.
% or less: ○, larger than that: ×
And so. Blow stretch molding conditions and bottle quality evaluation results are also shown in Table 1.
【表】
この結果から、本発明方法により得られたボト
ル(No.7)は、すでべての特性において優れてい
ることがわかる。
(発明の効果)
本発明によれば、適温に維持された金型内でパ
リソンを高温高速延伸することにより、熱収縮が
小さく形状が正確なボトルを高能率で製造するこ
とができる。[Table] From the results, it can be seen that the bottle (No. 7) obtained by the method of the present invention is already excellent in all properties. (Effects of the Invention) According to the present invention, by stretching a parison at high temperature and high speed in a mold maintained at an appropriate temperature, a bottle with a small thermal shrinkage and an accurate shape can be manufactured with high efficiency.
Claims (1)
リソンをブロー延伸成形して二軸配向ボトルを製
造する方法において、有底筒状パリソンを加熱し
て110〜125℃とし、そのパリソンを、表面が80〜
110℃に維持された金型内において、25000%/分
以上の延伸速度で延伸し、得られたボトルを引き
続き前記金型に押圧しつつ保持した後、金型から
離型することを特徴とするポリエステルボトルの
製造方法。1 In a method for producing a biaxially oriented bottle by blow-stretching a parison of ethylene terephthalate polyester, a bottomed cylindrical parison is heated to 110 to 125°C, and the parison is heated to a temperature of 80 to 125°C.
The bottle is stretched at a stretching speed of 25,000%/min or more in a mold maintained at 110°C, and the resulting bottle is held while being pressed against the mold, and then released from the mold. A method for manufacturing polyester bottles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60215671A JPS6274622A (en) | 1985-09-28 | 1985-09-28 | Manufacture of polyester bottle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60215671A JPS6274622A (en) | 1985-09-28 | 1985-09-28 | Manufacture of polyester bottle |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6274622A JPS6274622A (en) | 1987-04-06 |
| JPH058087B2 true JPH058087B2 (en) | 1993-02-01 |
Family
ID=16676237
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60215671A Granted JPS6274622A (en) | 1985-09-28 | 1985-09-28 | Manufacture of polyester bottle |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6274622A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6359513A (en) * | 1986-08-30 | 1988-03-15 | Toyo Seikan Kaisha Ltd | Manufacture of hollow polyester molded body |
-
1985
- 1985-09-28 JP JP60215671A patent/JPS6274622A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6274622A (en) | 1987-04-06 |
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