JPH0326646B2 - - Google Patents

Info

Publication number
JPH0326646B2
JPH0326646B2 JP58108885A JP10888583A JPH0326646B2 JP H0326646 B2 JPH0326646 B2 JP H0326646B2 JP 58108885 A JP58108885 A JP 58108885A JP 10888583 A JP10888583 A JP 10888583A JP H0326646 B2 JPH0326646 B2 JP H0326646B2
Authority
JP
Japan
Prior art keywords
heating
spout
preform
temperature
section
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
JP58108885A
Other languages
Japanese (ja)
Other versions
JPS60927A (en
Inventor
Kohei Sugano
Tatsuo Oonishi
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 Chemical Corp
Original Assignee
Mitsubishi Plastics Industries 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 Plastics Industries Ltd filed Critical Mitsubishi Plastics Industries Ltd
Priority to JP58108885A priority Critical patent/JPS60927A/en
Publication of JPS60927A publication Critical patent/JPS60927A/en
Publication of JPH0326646B2 publication Critical patent/JPH0326646B2/ja
Granted legal-status Critical Current

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
    • B29C49/64—Heating or cooling preforms, parisons or blown articles
    • B29C49/6409—Thermal conditioning of preforms
    • 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
    • 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
    • B29C49/64—Heating or cooling preforms, parisons or blown articles
    • B29C49/6409—Thermal conditioning of preforms
    • B29C49/6418—Heating of preforms
    • 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
    • B29C49/64—Heating or cooling preforms, parisons or blown articles
    • B29C49/6409—Thermal conditioning of preforms
    • B29C49/6436—Thermal conditioning of preforms characterised by temperature differential
    • B29C49/6445—Thermal conditioning of preforms characterised by temperature differential through the preform length
    • B29C49/6452—Thermal conditioning of preforms characterised by temperature differential through the preform length by heating the neck
    • 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
    • B29C49/64—Heating or cooling preforms, parisons or blown articles
    • B29C49/6472—Heating or cooling preforms, parisons or blown articles in several stages
    • B29C49/648—Heating or cooling preforms, parisons or blown articles in several stages of preforms or parisons

Landscapes

  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、ポリエステル樹脂ブローボトルまた
はプリフオームの口栓部を加熱して結晶化させる
方法に関するものである。 ポリエステル樹脂ブローボトルの口栓部に耐熱
性を付与するために、ブローボトルまたは該ブロ
ーボトルを成形するためのプリフオームの段階で
口栓部を加熱して結晶化させることが行なわれて
いる。ところが従来の加熱方法では、高い加熱温
度で加熱するとプリフオーム成形時に残留した内
部歪が回復して口栓部の天面やねじ部が波状に変
形するために、キヤツプによる密封が不完全にな
る問題があつた。また一方、変形を避けるために
加熱温度を下げると結晶化させるに要する時間が
長くなり、製造効率が低下する。 本発明は、上記問題点を解決し変形がなく、し
かも効率的に口栓部を結晶化させることを目的と
し、その要旨は、ポリエステル樹脂ブローボトル
または該ブローボトルを成形するためのプリフオ
ームの口栓部を加熱して結晶化させる方法におい
て、加熱を複数の段階に分け、第1段階で低い加
熱温度で徐々に加熱し、引き続き第2段階で加熱
温度を高めて加熱結晶化することを特徴とする口
栓部の結晶化方法である。 上記のように加熱を複数の段階に分け、第1段
階で低い加熱温度で徐々に加熱することにより、
口栓部が変形せずに内部歪が除去される効果があ
る。そして引き続き第2段階で加熱温度を高めて
加熱するので第1段階で予備的に昇温されている
こととあいまつて充分な結晶化速度で迅速に結晶
化させることができ、しかも内部歪は第1段階で
除去されているので口栓部が変形しない。 第1段階における加熱温度としてはプリフオー
ムの成形条件、肉厚等により相違するが、ポリエ
チレンテレフタレート樹脂製のほぼ室温の口栓部
を、口栓部自体の温度で100〜120℃に15〜40秒で
徐々に到達させることができる程度が口栓部の変
形がなく、予備的な加熱としても充分なので好ま
しい。 第2段階では、第1段階に引き続き加熱温度を
高めて20〜40秒で口栓部が160〜180℃に到達させ
るようにするのが、好ましい。このような加熱条
件では第1段階の加熱開始から通常100秒以内に、
口栓部の結晶化度は30%に到達し耐熱性が改良さ
れる。 本発明においてポリエステル樹脂製のプリフオ
ームまたはブローボトルは、ポリエチレンテレフ
タレートあるいはエチレンテレフタレートを主た
る繰り返し単位とする共重合体等のポリエステル
樹脂を射出成形、押出成形等により管状に成形し
たプリフオームまたはこのようなプリフオームを
ポリエステル樹脂のガラス転移温度以上、溶融温
度以下の温度範囲で二軸延伸ブロー成形したボト
ルが好適に用いられる。このボトルは口栓部以外
の部分をあらかじめ熱固定してあつてもよい。 次に添付図面に基づいて説明するに、第1図
は、本発明のボトル口栓部の結晶化方法を実施す
るための加熱装置の一例を示す概略平面図、第2
図は第1図の−断面の拡大図である。 第1〜2図に示すように加熱装置全体は3つの
区間a、b、cに分かれており、それぞれの区間
に相対向して一対ずつの棒状の近赤外線ヒーター
1a,1b,1cが設置されている。そしてこれ
らのヒーターの間を自転しながら矢印A方向に移
動する、マンドレル2が配置される。さらにヒー
ターの上方には口栓部以外に熱がかからぬように
遮熱板3が設置されている。ヒーター1a,1
b,1cはそれぞれ独立して、電流を調節して加
熱温度を制御できるようにしてある。マンドレル
2は第2図に示すように、プリフオーム等の口栓
部4の内径に適合する径を有し、プリフオームに
挿入した状態で移送し、加熱中に口栓部4の変形
を内面から規制するものである。なおマンドレル
2は、ポリ4・フツ化・エチレン、ポリアセター
ル、ポリアミド、ポリカーボネート、ポリプロピ
レン等の耐熱性プラスチツクで製造するか被覆す
れば、金属製のものに比べて表面のすべりが良
く、プリフオーム等の挿入、引き抜きがスムーズ
となる。またマンドレル2の上方に、プリフオー
ム等の内底面に接してプリフオームの自重を支え
る支持棒21を設けてもよい。 ヒーター1a,1b,1cとしては図に示すよ
うな赤外線ヒーター等の棒状のもののほか、高周
波電極による誘導加熱、熱風加熱、接触加熱また
はこれらの組合せ等実質的に加熱温度を制御でき
るものであれば適宜の方法を用いることができ
る。 以上説明したように、本発明によればポリエス
テル樹脂ブローボトルまたはそのプリフオームの
口栓部を、第1段階で低い加熱温度で加熱して
後、引続き加熱温度を高めて加熱・結晶化させる
ので、口栓部の変形が生ずることなく、しかも迅
速に結晶化させることができる。 以下実験例によりさらに詳細に説明する。 実験例 第1図の様に配置された加熱装置を用いて口栓
部4の長さ22.4mm、ねじ山径28mm、内径21.6mmの
ポリエチレンテレフタレート製プリフオームを加
熱した。加熱ヒーター1a,1b,1cは、いず
れも近赤外線ヒーター(200V、1K.W.、長さ35
cm)を使用している。 マンドレル2により移送されるプリフオームの
各区間の通過時間はいずれも30秒ずつである。 この装置において、第1表No.1〜10に示すよう
にヒーター電流をa区間を1.1アンペア〜3.5アン
ペア、b区間を3.5アンペア、c区間4.0〜2.0アン
ペアの範囲で調整することにより加熱温度を制御
し、マンドレル2にプリフオームを差し込んで3
区間を通過させ、口栓部4を外観的に充分白化
(結晶化度30%以上)するまで結晶化させた。 結晶化の終了したプリフオームについて、口栓
部4の天面41の凹凸を読取顕微鏡により観察
し、凹部と凸部の差が0.1mm以上のものを不良と
判定し、第1表に示すNo.1〜10の各条件、200本
ずつテストして、不良本数を表示した。
The present invention relates to a method of heating and crystallizing the spout of a polyester resin blow bottle or preform. In order to impart heat resistance to the spout of a polyester resin blow bottle, the spout is heated and crystallized at the stage of the blow bottle or a preform for molding the blow bottle. However, with conventional heating methods, when heated at a high heating temperature, the internal strain remaining during preform molding recovers, causing the top surface and threaded portion of the spout to become wavy, resulting in incomplete sealing by the cap. It was hot. On the other hand, if the heating temperature is lowered in order to avoid deformation, the time required for crystallization becomes longer and manufacturing efficiency decreases. The object of the present invention is to solve the above-mentioned problems and to efficiently crystallize the spout part without deformation. A method of heating and crystallizing a stopper part is characterized by dividing the heating into multiple stages, gradually heating at a low heating temperature in the first stage, and then increasing the heating temperature in the second stage to perform heating crystallization. This is a method of crystallizing a spout. By dividing heating into multiple stages as described above and gradually heating at a low heating temperature in the first stage,
This has the effect of eliminating internal strain without deforming the plug portion. Then, in the second stage, the heating temperature is raised and the heating is carried out, so combined with the preliminary temperature increase in the first stage, it is possible to quickly crystallize at a sufficient crystallization rate, and the internal strain is reduced even further. Since it is removed in one step, the spout does not deform. The heating temperature in the first stage varies depending on the preform molding conditions, wall thickness, etc., but the polyethylene terephthalate resin spout is heated to 100 to 120°C at the temperature of the spout itself for 15 to 40 seconds. It is preferable that the temperature can be gradually reached at 50° C. since the spout does not deform and is sufficient for preliminary heating. In the second stage, it is preferable to increase the heating temperature following the first stage so that the spout reaches 160 to 180°C in 20 to 40 seconds. Under such heating conditions, usually within 100 seconds from the start of the first stage heating,
The crystallinity of the spout reaches 30%, improving heat resistance. In the present invention, the preform or blow bottle made of polyester resin is a preform formed into a tubular shape by injection molding, extrusion molding, etc. of polyester resin such as polyethylene terephthalate or a copolymer having ethylene terephthalate as a main repeating unit, or a preform made of such a preform. A bottle biaxially stretched and blow-molded at a temperature range of not less than the glass transition temperature and not more than the melting temperature of the polyester resin is preferably used. This bottle may be heat-fixed in advance in parts other than the spout. Next, referring to the accompanying drawings, FIG. 1 is a schematic plan view showing an example of a heating device for carrying out the method of crystallizing a bottle cap of the present invention;
The figure is an enlarged view of the - cross section of FIG. 1. As shown in Figures 1 and 2, the entire heating device is divided into three sections a, b, and c, and a pair of rod-shaped near-infrared heaters 1a, 1b, and 1c are installed in each section facing each other. ing. A mandrel 2 is arranged between these heaters and moves in the direction of arrow A while rotating. Furthermore, a heat shield plate 3 is installed above the heater to prevent heat from being applied to areas other than the spout. Heater 1a, 1
b and 1c are arranged so that the heating temperature can be controlled by adjusting the current independently. As shown in Fig. 2, the mandrel 2 has a diameter that matches the inner diameter of the spout 4 of the preform, etc., and is transported while being inserted into the preform, and prevents deformation of the spout 4 from the inside during heating. It is something to do. If the mandrel 2 is made or coated with a heat-resistant plastic such as poly-4, fluoride, ethylene, polyacetal, polyamide, polycarbonate, or polypropylene, the surface will be smoother than a metal one, making it easier to insert the preform, etc. , pulling out becomes smooth. Further, a support rod 21 may be provided above the mandrel 2 in contact with the inner bottom surface of the preform etc. to support the weight of the preform. The heaters 1a, 1b, and 1c may be rod-shaped heaters such as infrared heaters as shown in the figure, as well as induction heating using high-frequency electrodes, hot air heating, contact heating, or combinations thereof, as long as the heating temperature can be substantially controlled. Any suitable method can be used. As explained above, according to the present invention, the spout of the polyester resin blow bottle or its preform is heated at a low heating temperature in the first step, and then heated and crystallized by increasing the heating temperature. Crystallization can be performed quickly without causing deformation of the plug portion. This will be explained in more detail below using experimental examples. Experimental Example A polyethylene terephthalate preform having a spout 4 having a length of 22.4 mm, a thread diameter of 28 mm, and an inner diameter of 21.6 mm was heated using a heating device arranged as shown in FIG. Heating heaters 1a, 1b, and 1c are all near-infrared heaters (200V, 1K.W., length 35
cm) is used. The time required for each section of the preform to be transported by the mandrel 2 is 30 seconds. In this device, the heating temperature can be adjusted by adjusting the heater current within the ranges of 1.1 amperes to 3.5 amperes in section a, 3.5 amperes in section b, and 4.0 to 2.0 amperes in section c, as shown in Table 1 Nos. 1 to 10. control, insert the preform into mandrel 2 and press 3.
The sample was allowed to pass through the section and crystallized until the spout 4 became sufficiently white in appearance (crystallinity of 30% or more). For the preform that has been crystallized, the irregularities on the top surface 41 of the spout portion 4 were observed using a reading microscope, and those with a difference of 0.1 mm or more between the concave and convex portions were determined to be defective, and No. 1 shown in Table 1 was determined. 200 pieces were tested under each condition from 1 to 10, and the number of defective pieces was displayed.

【表】【table】

【表】 第1表から明らかなように、No.1〜9で示すよ
うにa区間すなわち第1段階において比較的低い
加熱温度(3.3アンペア以下)で加熱したものは、
不良本数0〜36本と、最初から高温(3.5アンペ
ア)で加熱したもの(不良本数93本)より変形が
少ない。またa区間のヒーー電流をIa、b区間の
ヒーター電流をIbとした時に、a区間のb区間に
対する加熱能力PをIa2/Ib2×100(%)で表わす
と、Pが30%〜70%の間にあるNo.3〜7の条件は
不良本数が0〜3本と特に小さくなつており特に
好ましい。 なおc区間のヒーター電流を調整した目的は、
口栓部表面が加熱オーバーにより溶融しないよう
に、口栓部の昇温を抑えてほぼ一定温に保たれる
ように調整したものである。 また、a、b、cの各区間のヒーター電流をす
べて29アンペアと同一の加熱容量にして同様のテ
ストを行なうと、不良本数は0本であるが、c区
間を通過した時点で少し曇る程度の白化しか生ぜ
ず、結晶化の程度が小さかつた。
[Table] As is clear from Table 1, those heated at a relatively low heating temperature (3.3 amperes or less) in section a, that is, the first stage, as shown in Nos. 1 to 9,
The number of defective pieces ranged from 0 to 36, which resulted in less deformation than those that were heated at high temperatures (3.5 amperes) from the beginning (93 defective pieces). Also, when the heater current in section a is Ia and the heater current in section b is Ib, if the heating capacity P of section a to section b is expressed as Ia 2 /Ib 2 × 100 (%), then P is 30% to 70 Conditions Nos. 3 to 7, which are between % and 3, are particularly preferable because the number of defective pieces is particularly small, 0 to 3 pieces. The purpose of adjusting the heater current in section c is
In order to prevent the surface of the spout from melting due to overheating, the temperature rise of the spout is suppressed and the temperature is maintained at a substantially constant temperature. Also, if you perform a similar test with the heater current in each section a, b, and c at the same heating capacity of 29 amperes, the number of defective wires is 0, but there is only a slight clouding after passing through section c. Only whitening occurred, and the degree of crystallization was small.

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

第1図は本発明のボトル口栓部を結晶化方法を
実施するために装置の一例を示す概略平面図、第
2図は第1図の−断面の拡大図である。 1a,1b,1c……ヒーター、2……マンド
レル、3……遮熱板。
FIG. 1 is a schematic plan view showing an example of an apparatus for carrying out the method of crystallizing a bottle cap according to the present invention, and FIG. 2 is an enlarged cross-sectional view taken along the line -- in FIG. 1a, 1b, 1c...heater, 2...mandrel, 3...heat shield plate.

Claims (1)

【特許請求の範囲】[Claims] 1 ポリエステル樹脂ブローボトルまたは該ブロ
ーボトルを成形するためのプリフオームの口栓部
を加熱して結晶化させる方法において、加熱を複
数の段階に分け、第1段階で低い加熱温度で徐々
に加熱し、引き続き第2段階で加熱温度を高めて
加熱結晶化することを特徴とする口栓部の結晶化
方法。
1. A method of heating and crystallizing the spout of a polyester resin blow bottle or a preform for molding the blow bottle, in which heating is divided into multiple stages, and in the first stage, heating is gradually performed at a low heating temperature, A method for crystallizing a spout portion, which is characterized in that the heating temperature is subsequently increased in a second step to perform heating crystallization.
JP58108885A 1983-06-17 1983-06-17 Crystallizing method of mouth part of bottle Granted JPS60927A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58108885A JPS60927A (en) 1983-06-17 1983-06-17 Crystallizing method of mouth part of bottle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58108885A JPS60927A (en) 1983-06-17 1983-06-17 Crystallizing method of mouth part of bottle

Publications (2)

Publication Number Publication Date
JPS60927A JPS60927A (en) 1985-01-07
JPH0326646B2 true JPH0326646B2 (en) 1991-04-11

Family

ID=14496058

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58108885A Granted JPS60927A (en) 1983-06-17 1983-06-17 Crystallizing method of mouth part of bottle

Country Status (1)

Country Link
JP (1) JPS60927A (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4562320B2 (en) * 2001-06-29 2010-10-13 株式会社吉野工業所 Fast whitening method for synthetic resin containers
JP4478977B2 (en) * 2004-05-31 2010-06-09 株式会社吉野工業所 Thermal crystallization treatment method for preform mouthpiece
CN1984766B (en) * 2004-07-28 2012-01-25 东洋制罐株式会社 Thermal crystallization system of saturated polyester hollow body and its heating method
JP4552693B2 (en) * 2005-02-28 2010-09-29 株式会社吉野工業所 Core member for heat treatment of synthetic resin molded products
JP4775791B2 (en) * 2005-04-21 2011-09-21 株式会社吉野工業所 Preform holding jig and thermal crystallization treatment equipment
WO2011148879A1 (en) * 2010-05-28 2011-12-01 日精エー・エス・ビー機械株式会社 Preform opening crystallization method

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