JPS6315129B2 - - Google Patents
Info
- Publication number
- JPS6315129B2 JPS6315129B2 JP55095608A JP9560880A JPS6315129B2 JP S6315129 B2 JPS6315129 B2 JP S6315129B2 JP 55095608 A JP55095608 A JP 55095608A JP 9560880 A JP9560880 A JP 9560880A JP S6315129 B2 JPS6315129 B2 JP S6315129B2
- Authority
- JP
- Japan
- Prior art keywords
- sheet
- face plate
- oriented
- thermoforming
- producing
- 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
Links
- 238000003856 thermoforming Methods 0.000 claims description 21
- 238000010438 heat treatment Methods 0.000 claims description 14
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 11
- 238000005096 rolling process Methods 0.000 claims description 9
- 230000003746 surface roughness Effects 0.000 claims description 6
- 229920003002 synthetic resin Polymers 0.000 claims description 6
- 239000000057 synthetic resin Substances 0.000 claims description 6
- 229920001169 thermoplastic Polymers 0.000 claims description 6
- 239000004416 thermosoftening plastic Substances 0.000 claims description 6
- 238000002844 melting Methods 0.000 claims description 4
- 230000008018 melting Effects 0.000 claims description 4
- 230000000977 initiatory effect Effects 0.000 claims description 2
- 238000007493 shaping process Methods 0.000 claims description 2
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 238000000465 moulding Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 2
- 230000001771 impaired effect Effects 0.000 description 2
- 229920005672 polyolefin resin Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- -1 polypropylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 238000007665 sagging Methods 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 238000007666 vacuum forming Methods 0.000 description 1
- 230000037303 wrinkles Effects 0.000 description 1
Landscapes
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
Description
本発明は熱成形品の製造方法に関し、詳しくは
配向された熱可塑性合成樹脂シートを接触型面板
熱成形機で熱成形してなる表面光沢および透明性
の改善された容器等の熱成形品の製造方法に関す
る。
従来、食品容器、医薬品容器等としてポリスチ
レン、ポリ塩化ビニルシートを通常の圧空、真空
成形等の熱成形によつて得られたものが使用され
てきており、これ等樹脂はその成形性に優れ、且
つ製品の透明性も非常に優れたものである事は周
知の如くである。しかるに、近年、これ等樹脂成
形品においては、その耐熱性、衛生性、廃棄時の
焼却公害等が問題視されており、これらの樹脂と
異なり前記問題点がないような樹脂、即ち、ポリ
エチレン、ポリプロピレン等のポリオレフイン系
樹脂、ナイロン、ポリエステル等の樹脂のシート
を熱成形して成形品を作るような技術も開発され
ている。
しかしながら、前記いずれの樹脂においても熱
成形機として従来の接触型面板熱成形機を使用し
た場合においては透明性や表面光沢等が損われ
る。即ち、従来の接触型面板熱成形機では透明性
等を向上させるために加熱用面板等を平滑にする
とシートの加熱時、即ちシートを加熱用面板に接
触させた時にシートと加熱用面板との間に空気が
局所的に気泡の様に残存し、シートの加熱むらが
生じ、容器等の成形品上に模様となつて残る(こ
の状態をレインドロツプ現象又は雨滴現象と称し
ている)。そのため従来はこのレインドロツプ現
象を防止するために加熱用面板の表面をある程度
粗面化して空気を除去しやすくしている。
しかしながら加熱用面板の表面粗度が大きい
と、シート表面が荒れて透明性や表面光沢等が損
われ、これは特にポリオレフイン系樹脂において
顕著である。
本発明は、表面光沢ならびに透明性にすぐれた
容器等の熱成形品の製造方法を提供することを目
的とする。
本発明者等は上記問題点を解決するために鋭意
検討した結果、熱可塑性合成樹脂シートとして配
向シートを使用すると理由は不明であるが、シー
トの加熱用面板への接触むらが減少し、レインド
ロツプ現象が発生しにくい点に着目し、配向シー
トを使用することにより接触型面板熱成形機にシ
ート接触面のより平滑な加熱用面板を使用するこ
とができることを見出し本発明に到達した。
即ち、本発明は熱可塑性合成樹脂の配向シート
を接触型面板熱成形機で熱成形してなる容器等の
熱成形品の製造方法において、該接触型面板熱成
形機の接触加熱用面板の表面粗度(JIS B−
0601)が3S以下の平滑度に仕上げた成形機を使
用することにより飛躍的に透明性や表面光沢等を
向上せしめたものである。
本発明で使用する配向シートとは一軸に配向が
付与されたシートからなり、一軸の配向の場合、
好ましくは配向前のシート幅に対する配向後のシ
ート幅の減少率を10%以下に保持することにより
容器等の成形品の歪みや偏肉等も防止される。
上記配向シートの製造法の一例としてロール圧
延による方法を詳述する。すなわち本発明は通常
の方法で熱可塑性合成樹脂シートを得、これをそ
の融点より低いか又はその流動開始点以下の温度
において互いに反対方向へ回転せしめられ、且つ
該シートの厚さよりも小さい間隔に設定された一
対の圧延ロール間隙を通過させる事により配向シ
ートが得られる。
又、この圧延処理に用いるシートはどんな成形
法で得られたものでもよく何等限定されない。即
ち通常用いられる押出し成形法でも良いし、又プ
レス成形、カレンダー成形等の方法を用いても差
支えない。かようなシートを圧延処理して熱成形
用シートとするのであるが、該シートの厚さはこ
れも本質的に限定されるものではないが、通常、
最終の圧延シート厚としては0.02mm〜2.0mmの範
囲が好ましく、特に0.1mm〜1.5mmが好ましい。過
度の厚さはロール圧延時の所要の圧延圧力が過大
となり圧延ロールは著しく大型とせざるを得ず、
経済的な観点から実施の有利性を判断せねばなら
ない。
又、ロール圧延の方法は従来公知の方法のいず
れでもよい。
かようにして作られた配向シートはレインドロ
ツプ現象が発生しにくいので熱成形機のシート接
触面をより平滑にする事が可能となり、該表面が
平滑性に優れる程、得られる成形品の透明性や表
面光沢等が良好な結果を与えるが、本発明の熱成
形機においては接触加熱用面板の表面粗度(JIS
試験法B−0601準拠)を3S以下とすべきである。
この場合金型の表面も平滑化する事によつて更に
好ましい結果を与える。
また、配向シートを接触型面板熱成形機により
賦形する時のシート温度は、該シートの融点又は
流動開始点より低い温度に維持することが好まし
い。
以上の如く本発明は配向シートを使用すること
によりレインドロツプ現象を回避し、飛躍的に透
明性、表面光沢性を向上させるばかりでなく、熱
成形時の予張り(予熱)時のシートのたるみ、し
わ等が発生せず、歪みや偏肉のない成形品が製造
される。
以下、本発明を実施例および比較例により具体
的に説明する。
実施例1〜2および比較例1〜4
第1表に示すごとく熱可塑性合成樹脂シートと
してiso−ポリプロピレン樹脂を用いて、特に実
施例1,2および比較例4においてはロール圧延
により配向を施した。このシートを表面粗度の異
なる加熱用面板を使用した接触型面板熱成形機
(金型表面粗度:5S)で熱成形し成形品(開口面
−170mm×100mm,深さ11mmの長方形トレイ)を得
た。なおシートと加熱用面板の接触時間は5秒と
し、また圧空圧5Kg/cm2とした。得られた成形品
の曇り価(HAZE VALUE)を測定し原反シー
トの曇り価と比較を行つた。また、この成形品の
レインドロツプ現象の発生の有無を調べた。結果
をそれぞれ第1表に示す。
The present invention relates to a method for producing thermoformed products, and more particularly to a method for producing thermoformed products such as containers with improved surface gloss and transparency, which are produced by thermoforming an oriented thermoplastic synthetic resin sheet using a contact type face plate thermoforming machine. Regarding the manufacturing method. Conventionally, polystyrene or polyvinyl chloride sheets obtained by thermoforming such as compressed air or vacuum forming have been used for food containers, pharmaceutical containers, etc., and these resins have excellent moldability. Furthermore, it is well known that the product has excellent transparency. However, in recent years, problems such as heat resistance, hygiene, and incineration pollution during disposal have been raised in these resin molded products. Techniques have also been developed for thermoforming sheets of resins such as polyolefin resins such as polypropylene, nylon, and polyester to produce molded products. However, for any of the above-mentioned resins, when a conventional contact type face plate thermoforming machine is used as a thermoforming machine, transparency, surface gloss, etc. are impaired. In other words, in conventional contact-type face plate thermoforming machines, if the heating face plate is smoothed to improve transparency, the contact between the sheet and the heating face plate is reduced when the sheet is heated, that is, when the sheet is brought into contact with the heating face plate. Air remains locally in the form of bubbles, causing uneven heating of the sheet and leaving a pattern on the molded product such as a container (this condition is called a raindrop phenomenon). Therefore, conventionally, in order to prevent this raindrop phenomenon, the surface of the heating face plate has been roughened to some extent to make it easier to remove air. However, if the surface roughness of the heating face plate is large, the sheet surface becomes rough and transparency, surface gloss, etc. are impaired, and this is particularly noticeable in polyolefin resins. An object of the present invention is to provide a method for manufacturing thermoformed products such as containers that have excellent surface gloss and transparency. As a result of intensive studies to solve the above problems, the inventors of the present invention found that using an oriented sheet as a thermoplastic synthetic resin sheet reduces uneven contact of the sheet to the heating face plate and reduces raindrops, although the reason is unknown. Focusing on the fact that this phenomenon is less likely to occur, the inventors have discovered that by using an oriented sheet, a heating face plate with a smoother sheet contact surface can be used in a contact type face plate thermoforming machine, and the present invention has been achieved. That is, the present invention provides a method for manufacturing a thermoformed product such as a container by thermoforming an oriented sheet of thermoplastic synthetic resin with a contact type face plate thermoforming machine, in which the surface of the contact heating face plate of the contact type face plate thermoforming machine is Roughness (JIS B-
0601) has dramatically improved transparency and surface gloss by using a molding machine that finishes the product to a smoothness of 3S or less. The oriented sheet used in the present invention consists of a sheet uniaxially oriented, and in the case of uniaxially oriented,
Preferably, by keeping the reduction rate of the sheet width after orientation to the sheet width before orientation to 10% or less, distortion and uneven thickness of molded products such as containers can be prevented. As an example of the method for manufacturing the above-mentioned oriented sheet, a method using roll rolling will be described in detail. That is, the present invention obtains a thermoplastic synthetic resin sheet by a conventional method, and rotates the sheet in opposite directions at a temperature lower than its melting point or below its flow initiation point, and at intervals smaller than the thickness of the sheet. An oriented sheet is obtained by passing through a set gap between a pair of rolling rolls. Further, the sheet used in this rolling process may be obtained by any molding method and is not limited in any way. That is, a commonly used extrusion molding method may be used, or a method such as press molding or calendar molding may be used. Such a sheet is rolled to form a thermoformable sheet, and the thickness of the sheet is not essentially limited, but usually
The final rolled sheet thickness is preferably in the range of 0.02 mm to 2.0 mm, particularly preferably 0.1 mm to 1.5 mm. If the thickness is excessive, the required rolling pressure during roll rolling will be excessive, and the rolling rolls will have to be extremely large.
The advantage of implementation must be judged from an economic perspective. Further, the rolling method may be any conventionally known method. Since the oriented sheet made in this way is less likely to cause raindrop phenomenon, it is possible to make the contact surface of the sheet in the thermoforming machine smoother, and the smoother the surface, the better the transparency of the resulting molded product. However, in the thermoforming machine of the present invention, the surface roughness of the contact heating face plate (JIS
(according to Test Method B-0601) should be 3S or less.
In this case, a more favorable result can be obtained by smoothing the surface of the mold. Further, the sheet temperature when shaping the oriented sheet using a contact type face plate thermoforming machine is preferably maintained at a temperature lower than the melting point or flow start point of the sheet. As described above, by using an oriented sheet, the present invention not only avoids the raindrop phenomenon and dramatically improves transparency and surface gloss, but also prevents sagging of the sheet during pre-stretching (preheating) during thermoforming. A molded product is produced without wrinkles, distortion, or uneven thickness. Hereinafter, the present invention will be specifically explained with reference to Examples and Comparative Examples. Examples 1 to 2 and Comparative Examples 1 to 4 As shown in Table 1, iso-polypropylene resin was used as the thermoplastic synthetic resin sheet, and in particular, in Examples 1 and 2 and Comparative Example 4, the sheets were oriented by roll rolling. . This sheet is thermoformed using a contact-type face plate thermoforming machine (mold surface roughness: 5S) that uses heating face plates with different surface roughness to form a molded product (a rectangular tray with an opening surface of -170 mm x 100 mm and a depth of 11 mm). I got it. The contact time between the sheet and the heating face plate was 5 seconds, and the air pressure was 5 kg/cm 2 . The haze value (HAZE VALUE) of the obtained molded article was measured and compared with the haze value of the original fabric sheet. In addition, the presence or absence of raindrop phenomenon in this molded article was investigated. The results are shown in Table 1.
【表】
第1表から明らかなように一軸配向シートを用
いて、かつ表面粗度の小さい加熱用面板を使用し
た接触型面板熱成形機により熱成形された成形品
はレインドロツプ現象が生じることがなく、また
容器壁の曇り価も小さい。[Table] As is clear from Table 1, the raindrop phenomenon may occur in molded products thermoformed by a contact type face plate thermoforming machine that uses a uniaxially oriented sheet and a heating face plate with a small surface roughness. In addition, the haze value on the container wall is low.
Claims (1)
機で熱成形してなる熱成形品の製造方法におい
て、該シートとして一軸配向シートを用い、かつ
該接触型面板熱成形機の加熱用面板の表面粗度が
3S以下の平滑度に仕上げられたことを特徴とす
る、前記熱成形品の製造方法。 2 前記配向シートの幅減少率(配向前のシート
幅に対する配向後のシート幅の減少率)が10%以
下である前記特許請求の範囲第1項記載の熱成形
品の製造方法。 3 前記配向シートがシートの融点又は流動開始
点より低い温度でロール圧延によつて配向された
一軸配向シートである、前記特許請求の範囲第1
項又は第2項記載の熱成形品の製造方法。 4 賦形時のシート温度を該シートの融点又は流
動開始点より低い温度に維持し、熱成形する、前
記特許請求の範囲第1項、第2項又は第3項記載
の熱成形品の製造方法。[Scope of Claims] 1. A method for producing a thermoformed article by thermoforming a thermoplastic synthetic resin sheet using a contact type face plate thermoforming machine, wherein a uniaxially oriented sheet is used as the sheet, and the contact type face plate thermoforming machine The surface roughness of the heating face plate is
The method for producing the thermoformed product, characterized in that the product is finished to a smoothness of 3S or less. 2. The method for producing a thermoformed article according to claim 1, wherein the width reduction rate of the oriented sheet (the reduction rate of the sheet width after orientation relative to the sheet width before orientation) is 10% or less. 3. Claim 1, wherein the oriented sheet is a uniaxially oriented sheet oriented by roll rolling at a temperature lower than the melting point or flow initiation point of the sheet.
A method for producing a thermoformed article according to item 1 or 2. 4. Production of a thermoformed article according to claim 1, 2, or 3, wherein the sheet temperature during shaping is maintained at a temperature lower than the melting point or flow start point of the sheet, and thermoforming is performed. Method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9560880A JPS5722012A (en) | 1980-07-15 | 1980-07-15 | Production of thermally formed article |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9560880A JPS5722012A (en) | 1980-07-15 | 1980-07-15 | Production of thermally formed article |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5722012A JPS5722012A (en) | 1982-02-04 |
JPS6315129B2 true JPS6315129B2 (en) | 1988-04-04 |
Family
ID=14142260
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9560880A Granted JPS5722012A (en) | 1980-07-15 | 1980-07-15 | Production of thermally formed article |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5722012A (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ZA794752B (en) * | 1978-09-29 | 1980-08-27 | Upjohn Co | Polymeric isocyanate binder with internal release agent |
JPS57110413A (en) * | 1980-12-29 | 1982-07-09 | Showa Denko Kk | Method and apparatus for subjecting polyolefine sheet to hot plate heating type air pressure heat molding |
JPS60229915A (en) * | 1984-04-28 | 1985-11-15 | Nippon Urethane Service:Kk | Resin composition for binder |
JPH0688816B2 (en) * | 1985-04-23 | 1994-11-09 | 東亞合成化学工業株式会社 | Cement quick setting agent |
JPH04323023A (en) * | 1991-04-23 | 1992-11-12 | Nippon Steel Corp | Manufacture of transparent polypropylene sheet |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53130768A (en) * | 1977-04-21 | 1978-11-15 | Nippon Petrochemicals Co Ltd | Production of transparent container |
-
1980
- 1980-07-15 JP JP9560880A patent/JPS5722012A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53130768A (en) * | 1977-04-21 | 1978-11-15 | Nippon Petrochemicals Co Ltd | Production of transparent container |
Also Published As
Publication number | Publication date |
---|---|
JPS5722012A (en) | 1982-02-04 |
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