JPH04118214A - Manufacture of transparent film, sheet or tube - Google Patents

Manufacture of transparent film, sheet or tube

Info

Publication number
JPH04118214A
JPH04118214A JP2237062A JP23706290A JPH04118214A JP H04118214 A JPH04118214 A JP H04118214A JP 2237062 A JP2237062 A JP 2237062A JP 23706290 A JP23706290 A JP 23706290A JP H04118214 A JPH04118214 A JP H04118214A
Authority
JP
Japan
Prior art keywords
temperature
die
film
resin
sheet
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.)
Granted
Application number
JP2237062A
Other languages
Japanese (ja)
Other versions
JP2993719B2 (en
Inventor
Toshio Taka
鷹 敏雄
Takao Okubo
卓男 大久保
Yoshimasa Saito
好正 斉藤
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.)
Resonac Holdings Corp
Original Assignee
Showa Denko KK
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 Showa Denko KK filed Critical Showa Denko KK
Priority to JP2237062A priority Critical patent/JP2993719B2/en
Publication of JPH04118214A publication Critical patent/JPH04118214A/en
Application granted granted Critical
Publication of JP2993719B2 publication Critical patent/JP2993719B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/625Screws characterised by the ratio of the threaded length of the screw to its outside diameter [L/D ratio]
    • 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
    • B29C48/92Measuring, controlling or regulating
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92609Dimensions
    • B29C2948/92647Thickness
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92704Temperature
    • 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
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92923Calibration, after-treatment or cooling zone

Landscapes

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

Abstract

PURPOSE:To make it possible to obtain film, sheet or tube remarkably excellent in transparency by a method wherein polyethylene-based resin is extruded in the form of molten film and, immediately after being heated so as to have the surface temperature, which is higher than the temperature of a die by 30 deg.C or more and, at the same time, not higher by 250 deg.C or more then the meeting point of resin, quenched. CONSTITUTION:As the polyethylene-based resin 4, low-density polyethylene is used so as to produce film having the thickness of 120mum with a 75mm diameter extruder (L/D=28) and a T-die having the width of 500mm in order to form at the take-off speed of 30m/sec with an air knife and a chill roll. In addition, an air gap was 300mm. In that case, the temperature of the T-die was 160 deg.C. The measured surface temperature of which were radiant-heated with a far infrared heater provided at the intermediate part between the T-die and the chill roll, was 250 deg.C. The above-mentioned molten film was quenched with the chill roll having the temperature of 20 deg.C so as to obtain film having the thickness of 120mum.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は透明性が極めてすぐれているフィルム、シート
またはチューブの製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a film, sheet or tube having extremely high transparency.

〔従来の技術1 一般に熱可塑性樹脂は押出機、ロールなどによって熱に
より容易に可塑化され、スリットを有するフラットまた
は円形のダイスより押出され、空気や水などの媒体によ
って冷却され、引取られて薄くなりながら固化する。一
般に使用されているポリエチレン系樹脂(たとえば、低
密度ポリエチレン樹脂)については、Tダイプロセスに
よってTダイスから押出され、エアーナイフ等によって
エアーでまず冷却されてから50〜60m/分の速度で
引取られながら水で冷却された回転しているチルロール
に密着することによって冷却され、固化している。この
さい、ポリエチレン系樹脂は結晶性のために結晶化する
。この過程において、一般に成形温度、すなわちポリエ
チレン系樹脂がダイスより押出される温度を高くすると
、急冷効果によって得られたフィルム、シートまたはチ
ューブの透明性は向上する。
[Prior art 1] In general, thermoplastic resins are easily plasticized by heat using an extruder, rolls, etc., extruded from a flat or circular die with slits, cooled by a medium such as air or water, and drawn off to form a thin film. It solidifies as it grows. Generally used polyethylene resins (for example, low-density polyethylene resins) are extruded from a T-die using the T-die process, cooled with air using an air knife, etc., and then taken off at a speed of 50 to 60 m/min. Meanwhile, it is cooled and solidified by coming into close contact with a rotating water-cooled chill roll. At this time, the polyethylene resin is crystallized due to its crystallinity. In this process, generally, when the molding temperature, that is, the temperature at which the polyethylene resin is extruded from the die, is increased, the transparency of the obtained film, sheet, or tube is improved due to the quenching effect.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

しかし、この押出の温度を余り高温にすると、該樹脂が
熱分解して酸化劣化などを生じ、コマーシャル的に昼夜
の連続運転を行なうと、押出機内に劣化物が付着し、偶
発的に押出されて製品(フィルム、シートまたはチュー
ブ)にゲルや黒点など発生し、製品の品質を著しく低下
させてしまう。
However, if the extrusion temperature is too high, the resin will thermally decompose, causing oxidative deterioration, and if the extruder is operated continuously day and night, deteriorated substances will adhere to the inside of the extruder, causing accidental extrusion. This causes gels and black spots to appear on the product (film, sheet, or tube), significantly reducing the quality of the product.

一方、製品のこれらの欠点を解決する(劣化を防止する
)ために成形温度を該樹脂が劣化しないように低い温度
に設定すると、急冷効果が不充分なために充分な冷却効
果が得られないという問題がある。とりわけ、熱安定性
が比較的によくない材料の加工などにおいてはこの影響
が大きかった。
On the other hand, if the molding temperature is set to a low temperature so that the resin does not deteriorate in order to solve these defects of the product (prevent deterioration), a sufficient cooling effect cannot be obtained because the rapid cooling effect is insufficient. There is a problem. In particular, this effect was significant when processing materials with relatively poor thermal stability.

これらのことから、本発明はこれらの欠点(間顕点)が
なく、すなわちポリエチレン系樹脂を使用して透明性が
極めてすぐれているフィルム。
For these reasons, the present invention is a film that does not have these drawbacks (intervening spots), that is, uses polyethylene resin and has extremely excellent transparency.

シートまたはチューブを得ることを目的とするものであ
る。
The purpose is to obtain sheets or tubes.

[課題を解決するための手段1 本発明者らは、前記課題を解決するため、鋭意研究を行
い、従来とは全く異なる考え方で、熱可塑性樹脂を低温
で溶融押出して、なお高温押出で成形した時以上の急冷
効果を出すことにより、従来得られなかった高透明で高
光沢のフィルム。
[Means for Solving the Problems 1] In order to solve the above-mentioned problems, the present inventors have conducted extensive research, and based on a concept completely different from conventional methods, they have developed a method of melt-extruding thermoplastic resins at low temperatures and then molding them by extrusion at high temperatures. A film with high transparency and high gloss that was previously unobtainable by producing a rapid cooling effect that exceeds that of the previous film.

シートまたはチューブが得られることを見出し。Heading that sheets or tubes are obtained.

本発明を完成させるに至った。The present invention has now been completed.

即ち本発明によれば、上記課題はポリエチレン系樹脂を
溶融押出してダイスより溶融膜を押出し、引取りながら
冷却してフィルム、シートまたはチューブを製造する方
法において、ダイスより押出された溶融膜がダイスから
冷却されて固化するまでの区間において、この溶融膜を
外部または内部より再度加熱して、溶融膜の表面温度が
ダイスの温度より30℃以上高く、且つ該樹脂の融点よ
りも250℃以上は高(ならない温度にしたのち、直ち
に急冷することを特徴とする透明性フィルム、シートま
たはチューブの製造方法によって解決することができる
That is, according to the present invention, the above problem is solved in a method of manufacturing a film, sheet or tube by melt extruding a polyethylene resin, extruding the molten film from a die, and cooling it while taking it. In the period between cooling and solidification, the molten film is heated again from the outside or inside so that the surface temperature of the molten film is 30°C or more higher than the die temperature and 250°C or more higher than the melting point of the resin. This problem can be solved by a method for manufacturing transparent films, sheets, or tubes, which is characterized by raising the temperature to a high temperature and then immediately quenching it.

以下、本発明を具体的に説明する。The present invention will be specifically explained below.

+11ポリエチレン系樹脂 本発明を適用できるポリエチレン系樹脂としては、エチ
レンのみでフリーラジカル触媒を使って製造されている
いわゆる高圧ポリエチレンr以下[ポリエチレン系樹脂
(A)」と云う]、エチレンを主成分とするα−オレフ
ィンとの共重合体〔以下[ポリエチレン系樹脂(B)」
と云う]およびエチレンを主成分とする他のモノマーと
の共重合体E以下[ポリエチレン系樹脂(C)]と云う
〕などが挙げられる。
+11 Polyethylene Resin Polyethylene resins to which the present invention can be applied include so-called high-pressure polyethylene R or lower [referred to as polyethylene resin (A)], which is produced using only ethylene and a free radical catalyst, and which has ethylene as its main component. copolymer with α-olefin [hereinafter referred to as [polyethylene resin (B)]
and copolymers E with other monomers containing ethylene as a main component (hereinafter referred to as polyethylene resin (C)).

これらのポリエチレン系樹脂はいずれも本発明を適用す
ることができるが、特に透明性の点で特徴を出すために
は0.935g / c rd未満の密度を有し、かつ
非品性の樹脂が望ましい。
The present invention can be applied to any of these polyethylene resins, but in order to obtain special characteristics in terms of transparency, resins that have a density of less than 0.935 g/c rd and are of poor quality are required. desirable.

さらに、本発明を適用できる樹脂としては前記ポリエチ
レン系樹脂(A)、ポリエチレン系樹脂(B)、ポリエ
チレン系樹脂fclをそれぞれ単独で用いても良いし、
混合して用いても良くまた積層して用いても良い。
Further, as resins to which the present invention can be applied, the polyethylene resin (A), polyethylene resin (B), and polyethylene resin fcl may each be used alone,
They may be used in a mixed manner or in a layered manner.

混合、積層の場合は、前記ポリエチレン系樹脂fAl 
、fB) 、 (C+相互の組合せでも良いし、相溶性
のある、又は密着性のある他の熱可塑性樹脂を混合又は
積層したものでも良い。これら混合又は積層に用いられ
る熱可塑性樹脂は0.935 g / c rn’以上
の密度を有するものでも良いが、混合又は積層体として
の全体の密度は0.935 g / c rn’以下と
なるようにすることが望ましい。
In the case of mixing and laminating, the polyethylene resin fAl
, fB) , (C+ may be a mutual combination, or may be a mixture or lamination of other compatible or adhesive thermoplastic resins.The thermoplastic resin used for these mixtures or laminations may be 0. Although it may have a density of 935 g/c rn' or more, it is desirable that the overall density as a mixture or laminate is 0.935 g/c rn' or less.

(2)フィルム、シートまたはチューブの製造前記のポ
リエチレン系樹脂を用いてフィルム、シートまたはチュ
ーブを製造するには、一般に行なわれている成形方法(
例えばTダイ法、インフレーション法、共押出法など)
が用いられる。いずれの場合でも成形温度は、使われる
ポリエチレン系樹脂や他の熱可塑性樹脂の種類によって
一概に規定するわけにはいかないが、使われる樹脂の融
点よりも20℃ないし130℃(好ましくは融点よりも
30℃ないし120℃)高い温度であれば良い。
(2) Production of films, sheets, or tubes In order to produce films, sheets, or tubes using the above-mentioned polyethylene resin, a commonly used molding method (
For example, T-die method, inflation method, coextrusion method, etc.)
is used. In either case, the molding temperature cannot be determined unconditionally depending on the type of polyethylene resin or other thermoplastic resin used, but it is between 20°C and 130°C above the melting point of the resin used (preferably above the melting point). A high temperature (30°C to 120°C) is sufficient.

本発明においては、上記成形温度でダイス等から押出さ
れた溶融膜が冷却されて固化するまでの区間において、
この溶融膜を外部または内部より再度加熱して、溶融膜
の表面温度をダイスの温度より高温にした後、ただちに
急冷することが重要である。この再加熱による溶融膜の
表面温度はダイスの温度より30℃以上高いことが望ま
しく、且つ、使われる樹脂の融点よりも250℃以上は
高くならない温度であることが望ましい。この温度がダ
イス温度より30℃以上高くないと本発明の効果が不十
分であり、一方便われる樹脂の融点よりも250℃以上
高い温度では、樹脂が熱分解したり、酸化劣化してしま
うので好ましくない。
In the present invention, in the section until the molten film extruded from a die etc. at the above molding temperature is cooled and solidified,
It is important to heat the molten film again from the outside or inside to make the surface temperature of the molten film higher than the temperature of the die, and then immediately cool it rapidly. The surface temperature of the molten film resulting from this reheating is desirably at least 30° C. higher than the temperature of the die, and desirably no higher than 250° C. above the melting point of the resin used. If this temperature is not 30°C or more higher than the die temperature, the effect of the present invention will be insufficient. On the other hand, if the temperature is 250°C or more higher than the melting point of the resin being used, the resin will thermally decompose or deteriorate due to oxidation. Undesirable.

再加熱の方法としては、ニクロムヒーター、セラミック
ヒータ−1遠赤外線ヒーターなどの輻射加熱方式が好ま
しい。
As a reheating method, a radiation heating method such as a nichrome heater or a ceramic heater-1 far infrared heater is preferable.

また、再加熱された溶融膜はただちに急冷されることが
必要であり、急冷法としては空冷法、水冷法があるが、
水冷法がより望ましい。
In addition, the reheated molten film must be immediately quenched, and quenching methods include air cooling and water cooling.
Water cooling method is more preferable.

本発明の方法が有効な理由は、輻射加熱方式によって膜
状態の樹脂を瞬間的に加熱するため、ダイスのような金
型での伝熱加熱に比し、はるかに高い温度に加熱しても
、樹脂の熱劣化が起らず急冷効果が大きくなるため、得
られるフィルム、シートまたはチューブの光沢が良く、
透明性が画期的に向上するのである。この効果について
は、以下の実施例で具体的に説明するが、本発明は実施
例に限定されるものでないことはいうまでもない。
The reason why the method of the present invention is effective is because the resin in the film state is instantaneously heated using a radiation heating method, so it can be heated to a much higher temperature compared to conductive heating in a mold such as a die. , the resulting film, sheet or tube has good gloss, as thermal deterioration of the resin does not occur and the rapid cooling effect increases.
Transparency will be dramatically improved. This effect will be specifically explained in the following examples, but it goes without saying that the present invention is not limited to the examples.

[実施例1 実施例、比較例で用いたポリエチレン系樹脂の物性を表
1に示す。また透明性の評価として、ヘイズ値はAST
M 01003−61 、グロス値はJIS 2874
11962にしたがってそれぞれ測定した。
[Example 1 Table 1 shows the physical properties of the polyethylene resin used in the Examples and Comparative Examples. In addition, as an evaluation of transparency, the haze value is AST
M 01003-61, gross value is JIS 2874
11962, respectively.

実施例1 ポリエチレン系樹脂(Al として表1に示した低密度
ポリエチレン(LDPE)を用い、75IIIIl押出
機(L/D=281 、幅500mmのTダイスを使用
して、厚み120μのフィルムをエアーナイフ、チルロ
ールにて引取速度30m/secで成形した。なおエア
ーギャップは300+amであった。ここでTダイス温
度は160℃で、Tダイスとチルロールの中間部分に遠
赤外線ヒーターを設置して、溶融膜の両側外側から輻射
加熱し、溶融膜の表面温度(外部加熱部の中央部でダイ
スより1OclI出た時のバブル温度)を測定したとこ
ろ250℃であった。
Example 1 Using low density polyethylene (LDPE) shown in Table 1 as a polyethylene resin (Al), a 120μ thick film was cut using an air knife using a 75III extruder (L/D=281, a T-die with a width of 500mm). The molding process was carried out using a chill roll at a take-up speed of 30 m/sec.The air gap was 300+ am.The T die temperature was 160°C, and a far infrared heater was installed between the T die and the chill roll to form the molten film. The surface temperature of the molten film (bubble temperature when 1 OclI comes out from the die at the center of the externally heated part) was measured to be 250°C.

この溶融膜を温度20℃のチルロールで急冷して120
LLのフィルムを得た。
This molten film was rapidly cooled with a chill roll at a temperature of 20°C.
A film of LL was obtained.

このようにして得られたフィルムの透明性の評価として
ヘイズ(%)およびクロス(%)を測定した。結果を表
2に示す。
Haze (%) and cross (%) were measured to evaluate the transparency of the film thus obtained. The results are shown in Table 2.

比較例1 実施例1において遠赤外線ヒーターによる加熱を行なわ
なかったことを除けば実施例1と同様の処理を行ってフ
ィルムを得た。結果を表2に示す。
Comparative Example 1 A film was obtained by carrying out the same treatment as in Example 1 except that heating with a far-infrared heater was not performed in Example 1. The results are shown in Table 2.

実施例2、比較例2 表1に示すポリエチレン系樹脂(8)を用い、厚み25
0μのシートを成形するためにダイス温度、溶融膜表面
温度を変えた以外はそれぞれ実施例1、比較例1と同様
の処理を行った。それぞれの条件および結果を表2に示
す。
Example 2, Comparative Example 2 Polyethylene resin (8) shown in Table 1 was used, and the thickness was 25 mm.
The same treatments as in Example 1 and Comparative Example 1 were carried out, except that the die temperature and molten film surface temperature were changed in order to form a 0μ sheet. Table 2 shows the respective conditions and results.

実施例3〜5 Tダイスの代りにインフレーション法を用い、チューブ
形成を行った例で、条件および結果を表2に示す。なお
実施例4は3層共押出による積層シートの例で、実施例
5は樹脂fA] と(8+のブレンドの例である。
Examples 3 to 5 Table 2 shows the conditions and results of tubes formed using the inflation method instead of T-dies. Note that Example 4 is an example of a laminated sheet produced by three-layer coextrusion, and Example 5 is an example of a blend of resins fA] and (8+).

比較例3〜5 実施例3〜5において、遠赤外線ヒーターによる加熱を
行なわなかった以外は、それぞれ実施例3〜5と同様で
ある。結果を表2に示す。
Comparative Examples 3 to 5 Examples 3 to 5 are the same as Examples 3 to 5, respectively, except that heating with a far-infrared heater was not performed. The results are shown in Table 2.

比較例6.7 比較例6.7は比較例1でTダイス温度を高めた場合に
相当する。
Comparative Example 6.7 Comparative Example 6.7 corresponds to Comparative Example 1 in which the T die temperature was increased.

表2より、比較例1.6の比較ではへイズ値がl015
%、6.5%と高温成形が明らかに透明性がすぐれてい
る事がわかる。しかし比較例7のようにTダイス温度が
270℃では樹脂が熱分解を起し安定成形が不可能とな
る。
From Table 2, in the comparison of Comparative Example 1.6, the haze value was 1015
%, 6.5%, and it can be seen that high-temperature molding clearly has superior transparency. However, when the T-die temperature is 270° C. as in Comparative Example 7, the resin undergoes thermal decomposition and stable molding becomes impossible.

一方、実施例ではダイス温度は比較的低くても忍融膜の
温度を高くすることにより、比較例にくらべいずれも透
明性が数段すぐれていることが明らかである。又溶融膜
の温度が300”Cでも熱分解を起すことなく安定的に
成形することが可能であった。
On the other hand, it is clear that in the Examples, even though the die temperature was relatively low, by increasing the temperature of the fused film, the transparency was much better than in the Comparative Examples. Furthermore, even when the temperature of the molten film was 300''C, stable molding was possible without causing thermal decomposition.

(以下余白) 〔発明の効果] 本発明の方法により、従来にくらべ透明性が極めてすぐ
れたフィルム、シートまたはチューブの製造が可能とな
った。
(Hereinafter in the margin) [Effects of the Invention] The method of the present invention has made it possible to produce films, sheets, or tubes with extremely superior transparency compared to conventional methods.

Claims (1)

【特許請求の範囲】[Claims] ポリエチレン系樹脂を溶融押出してダイスより溶融膜を
押出し、引取りながら冷却してフィルム、シートまたは
チューブを製造する方法において、ダイスより押出され
た溶融膜がダイスから冷却されて固化するまでの区間に
おいて、この溶融膜を外部または内部より再度加熱して
、溶融膜の表面温度がダイスの温度より30℃以上高く
、且つ該樹脂の融点よりも250℃以上は高くならない
温度にしたのち、直ちに急冷することを特徴とする透明
性フィルム、シートまたはチューブの製造方法。
In a method of manufacturing a film, sheet or tube by melt extruding polyethylene resin, extruding the molten film from a die, and cooling it while taking it, in the section where the molten film extruded from the die is cooled from the die and solidified. , This molten film is heated again from the outside or inside to a temperature where the surface temperature of the molten film is at least 30°C higher than the temperature of the die and no higher than 250°C higher than the melting point of the resin, and then immediately quenched. A method for producing a transparent film, sheet or tube, characterized by:
JP2237062A 1990-09-10 1990-09-10 Method for producing transparent film, sheet or tube Expired - Fee Related JP2993719B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2237062A JP2993719B2 (en) 1990-09-10 1990-09-10 Method for producing transparent film, sheet or tube

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2237062A JP2993719B2 (en) 1990-09-10 1990-09-10 Method for producing transparent film, sheet or tube

Publications (2)

Publication Number Publication Date
JPH04118214A true JPH04118214A (en) 1992-04-20
JP2993719B2 JP2993719B2 (en) 1999-12-27

Family

ID=17009857

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2237062A Expired - Fee Related JP2993719B2 (en) 1990-09-10 1990-09-10 Method for producing transparent film, sheet or tube

Country Status (1)

Country Link
JP (1) JP2993719B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012153030A (en) * 2011-01-27 2012-08-16 Hitachi Zosen Corp Method of molding eva resin sheet

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012153030A (en) * 2011-01-27 2012-08-16 Hitachi Zosen Corp Method of molding eva resin sheet

Also Published As

Publication number Publication date
JP2993719B2 (en) 1999-12-27

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