JPS62290516A - Corrugated tubular film and manufacture thereof - Google Patents

Corrugated tubular film and manufacture thereof

Info

Publication number
JPS62290516A
JPS62290516A JP61134295A JP13429586A JPS62290516A JP S62290516 A JPS62290516 A JP S62290516A JP 61134295 A JP61134295 A JP 61134295A JP 13429586 A JP13429586 A JP 13429586A JP S62290516 A JPS62290516 A JP S62290516A
Authority
JP
Japan
Prior art keywords
tube
take
tubular film
film
water
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.)
Pending
Application number
JP61134295A
Other languages
Japanese (ja)
Inventor
Masao Kurihara
正夫 栗原
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.)
Kurilon Chemicals Co Ltd
Original Assignee
Kurilon Chemicals 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 Kurilon Chemicals Co Ltd filed Critical Kurilon Chemicals Co Ltd
Priority to JP61134295A priority Critical patent/JPS62290516A/en
Publication of JPS62290516A publication Critical patent/JPS62290516A/en
Pending 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/90Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article
    • B29C48/901Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies
    • B29C48/903Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies externally
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B29C48/10Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/12Articles with an irregular circumference when viewed in cross-section, e.g. window profiles
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/13Articles with a cross-section varying in the longitudinal direction, e.g. corrugated pipes
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9115Cooling of hollow articles
    • B29C48/912Cooling of hollow articles of tubular films
    • B29C48/913Cooling of hollow articles of tubular films externally
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/919Thermal treatment of the stream of extruded material, e.g. cooling using a bath, e.g. extruding into an open bath to coagulate or cool the material

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

PURPOSE:To bring a novel visual effect to increase the visual value of a packed commodity and improve the working properties of bag making as well as bag- filling, by a method wherein, a tubular film is provided with corrugation by shaping continuous recesses and projections in the take-up direction thereof while cooling the film by water. CONSTITUTION:Air is sent into a molten synthetic resin tube 2, extruded from a die 1 with a diameter (a), through an air sending port 4 while passing it through an air ring 3 and providing a proper surface rigidity through cooling to inflate it until the diameter (b) is obtained, then, the tube 2 is passed through a water cooling ring 5 whereby the tube 2 is provided with a convergence. A multitude of flutes in the take-up direction of the same tube 2 is formed on the tube 2 by the convergence whereby the corrugated tubular film 2' with fine wave forms 2a may be obtained. The film 2' is passed further through a stabilizing plate 7, arranged below the water cooling ring 5, and is introduced into take-up rolls 8. The stabilizing plate 7 is constituted of two sheets of plate, which are opened at the introducing side of the corrugated tubular film 2' and closed at the take-up side of the same, while the film is reeled around a reeling roll 10 through the take-up rolls 8.

Description

【発明の詳細な説明】 3、発明の詳細な説明 産業上の利用分野 本発明は合成樹脂フィルムから成る各種包装袋、シート
状フィルム等の原材となる波賦形チューブ状フィルムと
その製法に関する。
[Detailed Description of the Invention] 3. Detailed Description of the Invention Industrial Application Field The present invention relates to a corrugated tubular film that is a raw material for various packaging bags, sheet films, etc. made of synthetic resin film, and a method for manufacturing the same. .

従来技術と問題点 一般に合成樹脂フィルムに凹凸形状を与える方法として
はフィルムに二次的に型押し加工し、然る後袋状にする
方法があるが、加工数が多くコスト高となり、型押しさ
れた平フィルムを9閉じする場合には側シール部を要し
美感を損なう。
Conventional technology and problems In general, there is a method to give a synthetic resin film an uneven shape by secondarily embossing the film and then forming it into a bag shape, but the number of processes is large and the cost is high. When the flat film is closed, a side seal portion is required, which impairs the aesthetic appearance.

又上記凹凸形状をチューブ状フィルムの成形時において
与える方法として特公昭46−第28668号が提供さ
れている。この先行例はダイより押出された溶融合成樹
脂チューブの冷却手段として金属冷却環体を用いるもの
であり、チューブの金属冷却環体通過時の接触部と非接
触部との冷却速度が異なることを利用したものである。
Furthermore, Japanese Patent Publication No. 1983-28668 provides a method for providing the above-mentioned uneven shape during molding of a tubular film. This prior example uses a metal cooling ring as a cooling means for a molten synthetic resin tube extruded from a die, and it is important to note that when the tube passes through the metal cooling ring, the cooling rate is different between the contact area and the non-contact area. It was used.

即ち冷却の遅い非接触部分に対し接触部は急冷固化され
るため、非接触部は接触部に比べ引取方向に対して伸長
されつつ多少長目に固化され、その長さの差にて同非接
触領域に引取り方向に直交した多数の漣状の変形が発生
することを原理としている。
In other words, since the contact part is rapidly cooled and solidified compared to the non-contact part, which cools slowly, the non-contact part is elongated and solidified somewhat longer in the drawing direction than the contact part, and the difference in length causes the same non-contact part to solidify. The principle is that a large number of ripple-shaped deformations occur in the contact area perpendicular to the pulling direction.

然しながらこの漣状の変形は仮に原理通りの現象が期待
できるとしても、一種の引きつれしわに相当するので、
見栄えが悪く外観を損なう、又不安定な冷却速度差や温
度差に依存するため常に均質に賦形することが難しい等
の技術的な問題をも有している。従って上記先行例では
チューブ状フィルムに引取方向と直行する漣状模様を付
加する手段、及び方法に関し開示しているが、工業上の
実施に難点がある。
However, even if this ripple-like deformation can be expected to occur in accordance with the principle, it is equivalent to a kind of wrinkled wrinkle.
It also has technical problems, such as being unsightly and spoiling the appearance, and being dependent on unstable cooling rate differences and temperature differences, making it difficult to form uniformly at all times. Therefore, although the above-mentioned prior art discloses a means and method for adding a ripple pattern perpendicular to the drawing direction to a tubular film, there are difficulties in industrial implementation.

発明の目的 本発明は包装袋として適用した場合の合成樹脂フィルム
の特徴を生かしつつ、更にその個性を増長させ独特の風
合を醸し出すことができるすだれ状の波賦形を施した新
規なチューブ状フィルムを提供する。この波賦形チュー
ブ状フィルムは包装袋等の原材として美感1機能両面に
おいて優れた特徴を具有するに至る。
Purpose of the Invention The present invention provides a novel tubular shape with a sash-like corrugated shape that takes advantage of the characteristics of a synthetic resin film when applied as a packaging bag, and further enhances its individuality and creates a unique texture. Provide film. This corrugated tubular film has excellent features in both aesthetics and function as a raw material for packaging bags and the like.

本発明は前記先行例の如き不安定要素、従って製造のネ
ックとなる冷却温度、同速度の差等を全く条件とせず、
既に実用面での裏づけを有する水冷固化法の利用による
単純な均一冷却にて予定の波賦形チューブ状フィルムが
容易に得られる製造法を提供する0本発明は前記先行例
のような引きつれじわを要素とする連成模様の賦形とは
全く異なり、引取方向に連続し且つ周方向に交互となる
賦形を有するチューブ状フィルムとその製法を提供する
The present invention does not require any unstable factors such as those in the preceding examples, such as differences in cooling temperature or cooling speed, which are bottlenecks in manufacturing.
The present invention provides a manufacturing method that allows a desired corrugated tubular film to be easily obtained by simple uniform cooling using a water-cooled solidification method that has already been proven in practical terms. To provide a tubular film having a shape that is continuous in the take-up direction and alternating in the circumferential direction, which is completely different from the shape of a continuous pattern with wrinkles as an element, and a method for producing the same.

本発明によって得られる波賦形チューブ状フィルムはこ
れを原材として形成される包装袋のイメージを御所する
もので、単なる包装手段としての側面からのみみられて
いた包装袋に対し被包装品の展示効果を倍化する効果を
付加し、しかも従来行われているインフレーションチュ
ーブの成形法の採用にて、その応用技術に関する着想の
付加にて目的の新規な波賦形チューブ状フィルムが簡単
に且つ再現性高く生産できるようにしたものである。
The corrugated tubular film obtained by the present invention has the image of a packaging bag made from it as a raw material, and unlike packaging bags that were seen only from the side as a mere packaging means, it is a product that can be packaged. In addition to doubling the exhibition effect, by adopting the conventional inflation tube forming method and adding an idea regarding its application technology, the desired new corrugated tubular film can be easily and easily produced. This allows for highly reproducible production.

発明の構成 而して1本発明はダイから押出された溶融合成樹脂チュ
ーブを水冷して形成するチューブ状フィルムであって、
該チューブ状フィルムに引取方向に連続する凹凸を水冷
賦形し波形にしだ波賦形チューブ状フィルムを提供する
Structure of the Invention The present invention is a tubular film formed by water-cooling a molten synthetic resin tube extruded from a die,
A corrugated tubular film is provided by water-cooling the tubular film to form concavities and convexities that are continuous in the drawing direction.

又本発明はダイから押出された溶融樹脂チューブを水冷
リングで冷却固化させるに際し、同チューブを膨張させ
ながらこれより小さな水冷リング内をA遇させるように
し、同チューブに収斂を与えると同時に該収斂溶融樹脂
チューブ全周を水冷リング内周に流出せる冷却水にて一
様に水冷固化させ全周に引取方向に連続する凹凸を賦形
し波形にするようにしだ波賦形チューブ状フィルムの製
法を提供する。
Further, in the present invention, when a molten resin tube extruded from a die is cooled and solidified in a water-cooled ring, the inside of the water-cooled ring, which is smaller than the tube, is expanded while the tube is expanded. A method for manufacturing a corrugated tubular film in which the entire circumference of the molten resin tube is uniformly water-cooled and solidified with cooling water that flows out to the inner circumference of the water-cooled ring, and the entire circumference is formed with concavities and convexities that continue in the drawing direction to create a corrugated shape. I will provide a.

本発明は上記によって目的の波賦形チューブ状フィルム
の提供を可能にしたものであって、これを図示した実施
例に基き説明すれば以下の通りである。
The present invention has made it possible to provide the desired corrugated tubular film as described above, and will be described below based on the illustrated embodiments.

発明の実施例 第1図に示すように1口径aのダイ1から押出した溶融
合成樹脂チューブ2を押出し直後にエヤーリング3内を
通して空冷し同チューブ2に適度な表面剛性を与えつつ
、ダイ1の中心に設けられた空気送入口4より空気を送
入して同チューブ2を直径すにまで膨張させ、この膨張
溶融合成樹脂チューブ2を水冷リング5内を通過させる
Embodiment of the Invention As shown in FIG. 1, a molten synthetic resin tube 2 extruded from a die 1 having a diameter of 1 is air-cooled through an air ring 3 immediately after extrusion to give the tube 2 an appropriate surface rigidity, and the die 1 is cooled. Air is introduced through an air inlet 4 provided at the center to expand the tube 2 to its diameter, and the expanded molten synthetic resin tube 2 is passed through a water cooling ring 5.

この水冷リング5は円筒形を呈し、上記膨張溶融合成樹
脂チューブ2の直径すより小径の直径Cを有する。他側
として水冷リング5を楕円形等とする。この場合も、上
記と同様水冷リング5の内周長を上記膨張溶融合成樹脂
チューブ2の円周長より小とする。
This water cooling ring 5 has a cylindrical shape and has a diameter C smaller than the diameter of the expanded molten synthetic resin tube 2. On the other side, the water cooling ring 5 has an oval shape or the like. In this case as well, the inner circumferential length of the water cooling ring 5 is made smaller than the circumferential length of the expanded molten synthetic resin tube 2 as described above.

上記の如くして膨張溶融合成樹脂チューブ2をこれより
小さな水冷リング5内へ通し、これに収斂を与える。こ
の収斂によって同チューブ2には引取り方向のヒダが周
方向に多数形成される。このヒダが後述の波賦形周期の
ピッチとなる。このヒダ及び波賦形周期のピッチは溶融
合成樹脂チューブ2の膨張度と水冷リング5の大きさの
差等による。
As described above, the expanded molten plastic tube 2 is passed through a smaller water cooling ring 5 to provide convergence. Due to this convergence, a large number of folds in the pulling direction are formed in the tube 2 in the circumferential direction. These folds become the pitch of the wave shaping period, which will be described later. The pitch of the pleats and wave shaping period depends on the difference between the degree of expansion of the molten synthetic resin tube 2 and the size of the water cooling ring 5.

上記の如く膨張溶融合成樹脂チューブ2へ水冷リング5
で収斂を与え、同時に該水冷リング5の全周において同
リング内周面側へ矢印で示す如く溢水流出させ、同収斂
チューブ全周を冷却水と直接接触せしめ、一様に急冷固
化させる。
As described above, the water cooling ring 5 is attached to the expanded molten synthetic resin tube 2.
At the same time, water is caused to overflow to the inner circumferential surface of the water cooling ring 5 as shown by the arrow, and the entire circumference of the convergence tube is brought into direct contact with cooling water to uniformly rapidly cool and solidify.

上記によって引取方向と平行なる凹凸を有し全体が縦方
向の谷と山から成る細かな波形2aになされた波賦形チ
ューブ状フィルム2′が得られる。
As a result of the above process, a corrugated tubular film 2' is obtained which has irregularities parallel to the drawing direction and is formed into fine corrugations 2a consisting of vertical valleys and peaks as a whole.

上記波賦形チューブ状フィルム2′はその波形2aの凹
凸が肉視的に全くバラツキを感じさせない振巾と周期を
持った整然とした外観を呈する。
The corrugated tubular film 2' has a regular appearance in which the unevenness of the corrugations 2a has an amplitude and a period that does not visually show any variation.

上記したエヤーリング3はそのエヤー吐出口をチューブ
取引方向に下り勾配となるように配向し、エヤー流をチ
ューブに直角に当てずに斜下方へ向はチューブに沿わせ
流す、このエヤーリング3によるチューブ表面への適度
な面剛性の付与はより鰭全なるヒダの形成に寄与する。
The air ring 3 described above has its air discharge port oriented downwardly in the tube trading direction, and the air flow does not hit the tube at right angles, but flows diagonally downward along the tube. Providing appropriate surface rigidity to the fin contributes to the formation of complete fin folds.

上記波賦形チューブ状フィルム2′を更に水冷リング5
の下位に配した安定板7を通し引取ロール8へ導入する
。安定板7は波賦形チューブ状フィルム2′の導入側に
おいて開き、導出側において閉じる二枚の板によって形
成され、同安定板7を通すことによって上記波賦形チュ
ーブ状フィルム2′を扁平に重ね折りし、引取ロール8
を経て、巻取ロール10に巻取る。上記安定板7の出口
側1例えば図示のように巻取りロール10の手前に実施
に応じ型押し成型ロール9を配し、扁平にされた波賦形
チューブ状フィルム2′を加熱しつつ、型押しして部分
的に波賦形を消去し、平坦部を部分的に形成する。この
平坦部は図形等であり、波賦形された波形2aと組合せ
て意匠効果を発揮する。
The above corrugated tubular film 2' is further heated by a water cooling ring 5.
It is introduced into the take-up roll 8 through the stabilizer plate 7 arranged below it. The stabilizing plate 7 is formed by two plates that open on the introduction side of the corrugated tubular film 2' and close on the outlet side, and flattens the corrugated tubular film 2' by passing the stabilizing plate 7 through it. Fold over and take over roll 8
After that, it is wound onto a take-up roll 10. An embossing molding roll 9 is disposed on the exit side 1 of the stabilizing plate 7, for example, in front of the take-up roll 10 as shown in the figure, and the flattened corrugated tubular film 2' is heated while being molded. Press to partially erase the wave shape and partially form a flat part. This flat portion is a figure or the like, and exhibits a design effect in combination with the waveform 2a.

上記の如くして得られた波賦形チューブ状フィルムを原
材とし、これを引取方向に等長に巾方向に切断し、第7
図に示すようにボトムシール2bを施すことによって包
装袋2″が得られる。この包装袋2″はチューブ状フィ
ルムの形態的特徴をそのまま保有しており、引取方向に
平行な谷と山とが周方向に規則的にすだれ状に形成され
た外観を呈し、この外観とその光反射効果がフィルム独
特の肌地合と相俟って、特異な意匠的効果を醸成する。
The corrugated tubular film obtained as described above was used as a raw material, and cut into equal lengths in the width direction in the take-up direction.
As shown in the figure, a packaging bag 2'' is obtained by applying the bottom seal 2b.This packaging bag 2'' retains the morphological characteristics of the tubular film, and has valleys and peaks parallel to the take-up direction. It has an appearance that is regularly formed in the shape of a blind in the circumferential direction, and this appearance and its light-reflecting effect, combined with the film's unique texture, create a unique design effect.

この時、上記ボトムシール2bは波形2aの保形に寄与
する。
At this time, the bottom seal 2b contributes to maintaining the shape of the waveform 2a.

実施例に付臭に言及すると、上記水冷リング5の水供給
手段としてその外周を囲むように水槽llを設け、該水
槽11へ冷却水人口12から冷却水6を常時一定流量で
供給することにより、水冷リング5の外側から内側へと
該供給量と等量の溢流を生じさせる。
Regarding odor addition in the embodiment, a water tank 11 is provided as a water supply means for the water cooling ring 5 so as to surround its outer periphery, and cooling water 6 is constantly supplied to the water tank 11 from a cooling water supply 12 at a constant flow rate. , causing an overflow from the outside of the water cooling ring 5 to the inside of the water cooling ring 5 in an amount equal to the amount supplied.

前記の如く該溢水は水冷リング5の内径により強制され
て収斂状態にある溶融合成樹脂チューブの外周面に沿い
膜状に落流し、その溢流直後の収斂チューブとの接触に
てこれを急冷固化せしめる。
As mentioned above, the overflowing water is forced by the inner diameter of the water cooling ring 5 to fall in a film form along the outer circumferential surface of the molten synthetic resin tube in a convergent state, and is rapidly cooled and solidified by contact with the convergent tube immediately after the overflow. urge

上記膨張溶融合成樹脂チューブ2は引取ロール3により
一定速度で引取ることにより、強制的により小なる水冷
リング5内へ引入れられ、そこで膨張量に応じた無数の
すだれ状ヒダを生成する。
The expanded molten synthetic resin tube 2 is taken up at a constant speed by a take-up roll 3, and is forcibly drawn into the smaller water-cooled ring 5, where it forms numerous interdigital folds corresponding to the amount of expansion.

このヒダは引取方向に直線的であり、且つ前記の如く周
方向に規則的であり、このすだれ状ヒダ形態が上記水冷
による急冷固化によりそのまま永久残留し、上記波賦形
がなされる。
These folds are linear in the take-up direction and regular in the circumferential direction as described above, and the interdigital folds remain permanently as they are by rapid solidification by the water cooling, resulting in the above-mentioned wavy shape.

実施例として上記水冷リング5を極めて低速で回動させ
る方法によって、上記波賦形はその回動速度に応じ引取
り方向に緩やかな螺旋状となる。
As an example, by rotating the water cooling ring 5 at an extremely low speed, the wave shape becomes a gentle spiral in the take-up direction depending on the rotation speed.

この波賦形は膨張溶融合成樹脂チューブ2の引取りに伴
ない、次々と波及しチューブ全長に亘る連bc1a模様
となる。この冷却固化は冷却水による直接接触冷却によ
るため、極めて急速に惹起され、水冷リング5の上端近
傍において、溶融状態から固化状態への変化が完了する
As the expanded molten synthetic resin tube 2 is taken up, this wave pattern spreads one after another, resulting in a continuous bc1a pattern extending over the entire length of the tube. Since this cooling and solidification is caused by direct contact cooling with cooling water, it occurs extremely rapidly, and the change from the molten state to the solidified state is completed near the upper end of the water cooling ring 5.

上記水冷リング5は第4図に断面形状を以って示すよう
に、膨張溶融合成樹脂チューブ2の導入口のリップ形状
を内側において鋭角となる尖鋭リップ5aとするか、又
は第5図に示すようにその内周面において上方に向は拡
大するようにテーパを付したテーパ付リップ5bとする
。 又上記水冷リング5は上記波形2aの形状又は配列
を規定する目的で、第6図A、Hに示すようにその導入
口のリップ内周縁部に周期的な溝5Cを形成することも
有効である。
The water cooling ring 5 has a lip shape at the inlet of the expanding molten synthetic resin tube 2, as shown in the cross-sectional shape in FIG. A tapered lip 5b is formed on the inner circumferential surface of the lip 5b so as to be tapered upwardly. It is also effective to form periodic grooves 5C in the inner peripheral edge of the lip of the inlet of the water cooling ring 5, as shown in FIGS. 6A and 6H, for the purpose of defining the shape or arrangement of the waveform 2a. be.

上記の如き波賦形における波形2aのピッチはダイlの
口径aと膨張溶融合成樹脂チューブ2の直径すと、水冷
リング5の内径C等の寸法、フィルムの厚み、引取り速
度等の要因で定まる。
The pitch of the waveform 2a in the above-mentioned wave shaping is determined by factors such as the diameter a of the die l, the diameter of the expanding molten synthetic resin tube 2, the inner diameter C of the water cooling ring 5, the thickness of the film, and the take-up speed. Determined.

溶融合成樹脂チユーブ2の直径すと水冷リング5の内径
Cとの比は1.10〜1.70の範囲内が適当である。
The ratio of the diameter of the molten synthetic resin tube 2 to the inner diameter C of the water cooling ring 5 is suitably within the range of 1.10 to 1.70.

 1.05以下では波形2aの賦形はできず、1.80
以上では波形2aの凹凸差が大きすぎて引取ロール部で
原反面に折り重なったしわが発生したり、波形2aの凹
凸の周期間隔が不規則になる恐れがある。
Waveform 2a cannot be shaped below 1.05, and 1.80
In this case, the difference in the unevenness of the waveform 2a is too large, and there is a risk that folded wrinkles may occur on the original surface at the take-up roll portion, or that the periodic intervals of the unevenness of the waveform 2a may become irregular.

最適な比の値は樹脂の種類、フィルムの厚み、引取り速
度等により相違するが、上記範囲で設定することにより
良好な波賦形がなされる。尚溶融合成樹脂チューブ2の
直径すがダイlの口径aより大きいことは必ずしも必要
ではない、baaであるような製造条件、所謂デフレ状
態であってもb / cを適切に設定することにより前
記波賦形が可ず駈である。
The optimum ratio value varies depending on the type of resin, the thickness of the film, the take-up speed, etc., but by setting it within the above range, good wave shaping can be achieved. It is not necessarily necessary that the diameter of the molten synthetic resin tube 2 is larger than the diameter a of the die l, but even under manufacturing conditions such as baa, so-called deflation, the above can be achieved by appropriately setting b/c. The wave shape is impossible and it is a cane.

次に上記説明に従いなされた本発明の実験例について述
べる。
Next, an experimental example of the present invention performed in accordance with the above explanation will be described.

実験例−1 低密度ポリエチレン樹脂を100腸■φの口径のダイよ
り押出し、樹脂チューブ径を70■膿φ程度に膨張させ
、内径54諺lφの水冷リングを引取速度13塵/分で
通過せしめ厚さ80終、折径85m1の原反をS!造し
たところ、引取方向に平行に連続する片面につき8周期
の凹凸形状が賦形された。
Experimental example-1 Low-density polyethylene resin was extruded through a die with a diameter of 100 cmφ, the resin tube diameter was expanded to about 70 mmφ, and the resin tube was passed through a water cooling ring with an inner diameter of 54 mm at a drawing speed of 13 particles/min. The original fabric with a thickness of 80 mm and a folded diameter of 85 m1 is S! When fabricated, a concavo-convex shape with eight periods was formed on one side that was continuous in parallel to the pulling direction.

実験例−2 インフレーション用ポリプロピレン樹脂ヲ100 mm
φの口径のダイより押出し、樹脂チューブ径851φ程
度に膨張させ、内径81m層φの水冷リングを引取速度
20■/分で通過せしめ、厚さ70#L、折径85膳1
の原反を製造したところ引取方向に平行に連続する片面
につき、13周期の凹凸形状が賦形された。
Experimental example-2 Polypropylene resin for inflation 100 mm
It was extruded from a die with a diameter of φ, expanded to a resin tube diameter of about 851φ, and passed through a water cooling ring with an inner diameter of 81 m layers at a take-up speed of 20 mm/min.
When the original fabric was produced, a concave and convex shape with 13 periods was formed on one side that was continuous in parallel to the take-up direction.

実験例−3 外層にインフレーション用ポリプロピレン樹脂、内層に
低密度ポリエチレン樹脂の二層組合せで外層25%、内
層75%の押出しffuii比で口径1001φの2層
ダイより押出し、樹脂チューブ径を120 ms+φ程
度に膨張させ、内径93mmφの水冷リングを引取速度
12層7分で通過せしめ厚さ801L、折径150m5
の原反を製造したところ、引取方向に平行に連続する片
面につき27周期の凹凸形状が賦形された。
Experimental example-3 A two-layer combination of inflation polypropylene resin for the outer layer and low-density polyethylene resin for the inner layer is extruded from a two-layer die with a diameter of 1001φ at an extrusion ffuii ratio of 25% for the outer layer and 75% for the inner layer, and the resin tube diameter is approximately 120 ms + φ. It was expanded to 801L in thickness and passed through a water-cooled ring with an inner diameter of 93mmφ at a take-up speed of 12 layers and 7 minutes, with a folded diameter of 150m5.
When the original fabric was manufactured, a concavo-convex shape with 27 periods was formed on one side that was continuous in parallel to the take-up direction.

実験例−4 外層にナイロン樹脂、中間層に変性ポリエチレン接着性
樹脂、内層に低密度ポリエチレンの3層組合せで外層3
5%、中間層20%、内層45%の押出し重量比で口径
120 @■φの3層ダイより押出し、樹脂チューブ径
を240 amφ程度に膨張させ、内径190 amφ
の水冷リングを引取速度13m/分で通過せしめ、厚さ
80IL、折径300m5の原反を製造したところ、引
取方向に平行に連続する片面につき60周期の凹凸形状
が賦形された。
Experimental example-4 Outer layer 3 is a combination of three layers: nylon resin for the outer layer, modified polyethylene adhesive resin for the middle layer, and low-density polyethylene for the inner layer.
5%, middle layer 20%, and inner layer 45% extrusion weight ratio through a three-layer die with a diameter of 120 @■φ, expand the resin tube diameter to about 240 amφ, and make an inner diameter of 190 amφ.
When a raw fabric with a thickness of 80 IL and a fold diameter of 300 m5 was produced by passing through a water-cooled ring at a take-up speed of 13 m/min, an uneven shape with 60 cycles was formed on one side that continued parallel to the take-up direction.

実験例−5 1記3層構成で口径80璽−φの3層ダイより押出し、
樹脂チューブ径を401φ程度に膨張させ、内径32m
5φの水冷リングを引取速度20■/分で通過せしめ、
厚さ80#L、折径50m腸の原反を製造したところ、
引取方向に平行に連続する片面につき16周期の凹凸形
状が賦形された。
Experimental example-5 Extrusion from a three-layer die with a diameter of 80 mm with the three-layer configuration described in 1.
Expand the resin tube diameter to about 401φ and make the inner diameter 32m.
It passes through a 5φ water cooling ring at a drawing speed of 20μ/min.
When we produced an original intestine with a thickness of 80 #L and a folded diameter of 50 m,
A concavo-convex shape with 16 cycles was formed on one side that continued parallel to the take-up direction.

発明の効果 本発明に係る波賦形チューブ状フィルムは縦方向の平行
な規則的な山部、谷部の形態付加に加え、フィルム肌地
合と相俟って、該形態付加による独特の光反射効果を生
み、従来の平チューブ状フィルムのイメージを御所する
特異な外観を醸成し、平チューブフィルムでは得られな
い斬新な視覚効果をもたらし、包装商品の視感価値を著
しく高揚し、種々の形態の包装手段として有効に活用で
きる。
Effects of the Invention The corrugated tubular film according to the present invention has regular parallel peaks and troughs in the longitudinal direction, and in combination with the film texture, it has a unique light effect due to the added shape. It creates a reflective effect, creates a unique appearance that echoes the image of conventional flat tube film, brings a novel visual effect that cannot be obtained with flat tube film, and significantly increases the visual value of packaged products. It can be effectively used as a form of packaging.

又、平チューブ状フィルムでは屡々見られる袋の内面間
の或は外面同志の密着現象がなく、更に上記周期的な波
賦形により袋の腰の強さが強化され、柔軟な素材でも適
度な剛性と直立性を具有させることができる等の効果を
もつ、これにより製袋加工適性や袋詰め作業適性、包装
機器に対する適合性が著しく改善される。
In addition, there is no phenomenon of close contact between the inner surfaces of the bag or between the outer surfaces, which is often seen with flat tubular films.Furthermore, the rigidity of the bag is strengthened by the above-mentioned periodic wave formation, and even flexible materials can be It has the effect of being able to have rigidity and uprightness, and as a result, suitability for bag making processing, suitability for bag filling work, and suitability for packaging equipment are significantly improved.

本発明は実験例で述べたように直接水冷インフレーショ
ン法により製造可能な単層又は多層の樹脂フィルムには
全て適用することができる。
As described in the experimental examples, the present invention can be applied to all single-layer or multi-layer resin films that can be produced by the direct water-cooling inflation method.

本発明法は特殊な設備を要することなく、在来のインフ
レーション成型設備の活用にて引取方向と平行に波賦形
されたチューブ状フィルムを量産でき、温度差等の難し
い設定を伴なわず、均質な波賦形を安定に形成できる。
The method of the present invention does not require any special equipment, and can mass-produce tubular films that are corrugated in parallel to the drawing direction by utilizing conventional inflation molding equipment, and does not involve difficult settings such as temperature differences. A homogeneous wave shape can be stably formed.

尚、本発明に係る引取方向に平行な周期的凹凸形状に賦
形された波賦形チューブ状フィルムはチューブ状のまま
製袋加工を行い、各種包装袋として使用できるばかりで
なく、切開いて平面的フィルムの原反としても使用でき
る。又自然色状態ばかりでなく着色剤を配合し着色原反
としても使用できる。
In addition, the corrugated tubular film according to the present invention, which is shaped into a periodic uneven shape parallel to the take-up direction, can be processed into bags as it is in the tube shape and used as various packaging bags, and can also be cut open and made into flat sheets. It can also be used as a base film for target films. In addition, it can be used not only in its natural color state but also as a colored original fabric by adding a coloring agent.

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

第1図は本発明製造法に実施する装置の概要を示す側面
図、第2図は波賦形チューブ状フィルムの要部を示す斜
視図、第3図A乃至り図は第1図のA−A’、B−B 
’、c−c ’、D−D’断面図、第4.第5図は水冷
リングの開口部形状の実施例を要部を以って示す断面図
、第6図Aは更に水冷リングの開口部形状の他側を示す
平面図、同B図は同要部断面図、第7図は波賦形チュー
ブ状フィルムを原材とする包装袋を一部切欠して示す側
面図である。 l・・・ダイ、2・・・溶融合成樹脂チューブ、2′・
・・波賦形チューブ状フィルム、2a・・・波形、5・
・・水冷リング、6・・・冷却水、a・・・ダイの口径
、b・・・膨張溶融合成樹脂チューブの直径、C・・・
水冷リングの内径。 特許出願人 クリロン化成株式会社 代理人 弁理視 中   畑    孝第1図 第2図 (C) 2”
FIG. 1 is a side view showing an outline of the apparatus used in the manufacturing method of the present invention, FIG. 2 is a perspective view showing the main parts of a corrugated tubular film, and FIGS. 3A to 3A are A of FIG. -A', B-B
', c-c', D-D' sectional view, 4th. FIG. 5 is a sectional view showing the main part of an embodiment of the opening shape of the water cooling ring, FIG. 6A is a plan view showing the other side of the opening shape of the water cooling ring, and FIG. FIG. 7 is a partially cutaway side view of a packaging bag made of corrugated tubular film as a raw material. l... die, 2... molten synthetic resin tube, 2'.
...Corrugated tubular film, 2a...Corrugated, 5.
...Water cooling ring, 6...Cooling water, a...Die diameter, b...Diameter of expanding molten synthetic resin tube, C...
Inner diameter of water cooling ring. Patent Applicant: Krylon Kasei Co., Ltd. Representative, Patent Attorney: Takashi Nakahata Figure 1 Figure 2 (C) 2”

Claims (2)

【特許請求の範囲】[Claims] (1)ダイから押出された溶融合成樹脂チューブを水冷
して形成するチューブ状フィルムであって、該チューブ
状フィルムに周方向に交互で且つ引取方向に連続する多
数の凹凸条を水冷賦形し波形にしたことを特徴とする波
賦形チューブ状フィルム。
(1) A tubular film formed by water-cooling a molten synthetic resin tube extruded from a die, in which a large number of uneven stripes are formed alternately in the circumferential direction and continuous in the drawing direction. A corrugated tubular film characterized by being corrugated.
(2)ダイから押出された溶融合成樹脂チューブを膨張
させながらこれより小さな水冷リング内を通過させて収
斂を与えると同時に、該収斂溶融合成樹脂チューブ全周
を氷冷リング内周に流出せる冷却水にて一様に水冷固化
させ全周に周方向に交互で且つ引取方向に連続する多数
の凹凸条を賦形し波形にすることを特徴とする波賦形チ
ューブ状フィルムの製法。
(2) While expanding the molten synthetic resin tube extruded from the die, it is passed through a smaller water-cooled ring to give convergence, and at the same time, the entire circumference of the converged molten synthetic resin tube is cooled to flow into the inner circumference of the ice-cooled ring. A method for producing a corrugated tubular film characterized by uniformly cooling and solidifying with water and forming a large number of concave and convex stripes on the entire circumference that are alternate in the circumferential direction and continuous in the drawing direction to form a corrugated shape.
JP61134295A 1986-06-10 1986-06-10 Corrugated tubular film and manufacture thereof Pending JPS62290516A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61134295A JPS62290516A (en) 1986-06-10 1986-06-10 Corrugated tubular film and manufacture thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61134295A JPS62290516A (en) 1986-06-10 1986-06-10 Corrugated tubular film and manufacture thereof

Publications (1)

Publication Number Publication Date
JPS62290516A true JPS62290516A (en) 1987-12-17

Family

ID=15124944

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61134295A Pending JPS62290516A (en) 1986-06-10 1986-06-10 Corrugated tubular film and manufacture thereof

Country Status (1)

Country Link
JP (1) JPS62290516A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4854163A (en) * 1971-11-10 1973-07-30
JPS5144150A (en) * 1974-08-01 1976-04-15 Akzo Nv
JPS5331181A (en) * 1976-07-30 1978-03-24 Gen Electric Electrostatic capacitance sensing device
JPS6189827A (en) * 1984-10-09 1986-05-08 Showa Denko Kk Inflation film molding method

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4854163A (en) * 1971-11-10 1973-07-30
JPS5144150A (en) * 1974-08-01 1976-04-15 Akzo Nv
JPS5331181A (en) * 1976-07-30 1978-03-24 Gen Electric Electrostatic capacitance sensing device
JPS6189827A (en) * 1984-10-09 1986-05-08 Showa Denko Kk Inflation film molding method

Similar Documents

Publication Publication Date Title
US5554093A (en) Flexible thermoplastic containers having a visual pattern thereon
JP2840498B2 (en) Method of linearizing the heat seal part in a plastic film zipper bag
US2750631A (en) Process for manufacturing ribbed extruded sheet material
US10265909B2 (en) Bag
US9272459B2 (en) Bag
US3857144A (en) Method of embossing limp plastic sheet material
KR100489474B1 (en) A mechenical fastener and a method for making a finger grip therefor
CN104540669B (en) The multilayer corrugation film formed by the discontinuous stacking of the film with different rebound degrees
US20160271864A1 (en) Thermoplastic films with visually-distinct stretched regions and methods for making the same
CN102224085A (en) Bag and method of making the same
CZ288923B6 (en) Cross-laminate and process for producing thereof
JPH0626852B2 (en) High-speed manufacturing method for web of debossed / porous thermoplastic film
US2718666A (en) Process of longitudinally stretching film of organic linear polymeric material
JPS5821576B2 (en) Net manufacturing method
JP6267359B2 (en) Method and apparatus for sealing together two webs of moving material having portions that are non-planar
US3393861A (en) Embossed thermoplastic bags
US4174416A (en) Tubular plastics material net having corrugations
JPS62290516A (en) Corrugated tubular film and manufacture thereof
EP0820856B1 (en) Perforated pre-streched strech film for pallet wrapping
US3664780A (en) Apparatus for making oriented webs
JP4566300B2 (en) Folding mold for plastic film and plastic film folding machine equipped with the folding mold
US10717226B2 (en) Agriculture storage bags and method to make same
US3736203A (en) Method of forming annular shaped wrapping
US7662450B2 (en) Ornamental ribbon and the process for its formation
JPH0735093B2 (en) T-die film, its manufacturing equipment, embossing roll and side seal bag