JPH10113985A - Manufacture of thermoplastic film - Google Patents
Manufacture of thermoplastic filmInfo
- Publication number
- JPH10113985A JPH10113985A JP8269752A JP26975296A JPH10113985A JP H10113985 A JPH10113985 A JP H10113985A JP 8269752 A JP8269752 A JP 8269752A JP 26975296 A JP26975296 A JP 26975296A JP H10113985 A JPH10113985 A JP H10113985A
- Authority
- JP
- Japan
- Prior art keywords
- film
- layer
- thickness
- stretched
- laminated film
- 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
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 14
- 229920001169 thermoplastic Polymers 0.000 title claims description 14
- 239000004416 thermosoftening plastic Substances 0.000 title claims description 14
- 239000010408 film Substances 0.000 claims abstract description 144
- 239000010409 thin film Substances 0.000 claims abstract description 11
- 238000009826 distribution Methods 0.000 claims abstract description 5
- 239000010410 layer Substances 0.000 claims description 42
- 239000002356 single layer Substances 0.000 claims description 12
- 238000001125 extrusion Methods 0.000 claims description 11
- 229920005992 thermoplastic resin Polymers 0.000 claims description 8
- 238000004804 winding Methods 0.000 claims description 7
- 239000011248 coating agent Substances 0.000 claims description 6
- 238000000576 coating method Methods 0.000 claims description 5
- 238000000034 method Methods 0.000 abstract description 12
- 230000000903 blocking effect Effects 0.000 abstract description 7
- 238000000227 grinding Methods 0.000 abstract description 3
- 230000002093 peripheral effect Effects 0.000 abstract description 2
- 229920005989 resin Polymers 0.000 description 17
- 239000011347 resin Substances 0.000 description 17
- 125000006850 spacer group Chemical group 0.000 description 11
- 229920000728 polyester Polymers 0.000 description 7
- -1 polyethylene Polymers 0.000 description 7
- 239000004952 Polyamide Substances 0.000 description 6
- 239000004721 Polyphenylene oxide Substances 0.000 description 6
- 229920002492 poly(sulfone) Polymers 0.000 description 6
- 229920002647 polyamide Polymers 0.000 description 6
- 229920000098 polyolefin Polymers 0.000 description 6
- 239000004743 Polypropylene Substances 0.000 description 5
- 238000001816 cooling Methods 0.000 description 5
- 238000009998 heat setting Methods 0.000 description 5
- 239000000853 adhesive Substances 0.000 description 4
- 230000001070 adhesive effect Effects 0.000 description 4
- 239000012790 adhesive layer Substances 0.000 description 4
- 229920006393 polyether sulfone Polymers 0.000 description 4
- 229920001155 polypropylene Polymers 0.000 description 4
- 239000002344 surface layer Substances 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 239000002313 adhesive film Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 238000010030 laminating Methods 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 229920000570 polyether Polymers 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 150000003457 sulfones Chemical class 0.000 description 2
- 229920002292 Nylon 6 Polymers 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- 239000004696 Poly ether ether ketone Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 229920001328 Polyvinylidene chloride Polymers 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 230000005250 beta ray Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000005001 laminate film Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229920001643 poly(ether ketone) Polymers 0.000 description 1
- 229920003207 poly(ethylene-2,6-naphthalate) Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 229920002530 polyetherether ketone Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 239000011112 polyethylene naphthalate Substances 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000005033 polyvinylidene chloride Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000009966 trimming Methods 0.000 description 1
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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion 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
- B29C48/07—Flat, e.g. panels
- B29C48/08—Flat, e.g. panels flexible, e.g. films
-
- 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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92009—Measured parameter
- B29C2948/92114—Dimensions
- B29C2948/92152—Thickness
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92323—Location or phase of measurement
- B29C2948/92438—Conveying, transporting or storage of articles
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92609—Dimensions
- B29C2948/92647—Thickness
-
- 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
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/92857—Extrusion unit
- B29C2948/92904—Die; Nozzle zone
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は2つ以上の熱可塑性
フィルムを一挙に製造する方法に関し、更に詳しくは2
つ以上のフィルムを厚み斑なく、また薄膜特に易接着薄
膜を塗設したフィルムを巻き取っる場合薄膜層同士のブ
ロッキング等のトラブルを回避する熱可塑性フィルムの
製造方法に関する。The present invention relates to a method for producing two or more thermoplastic films at once, and more particularly to a method for producing two or more thermoplastic films at once.
The present invention relates to a method for producing a thermoplastic film that avoids troubles such as blocking between thin film layers when winding a film coated with a thin film, particularly an easily adhesive thin film, with at least one film having no thickness unevenness.
【0002】[0002]
【従来の技術】熱可塑性樹脂からなる複数のフィルムを
生産性向上の目的で一挙に製造する方法として、剥離用
スペーサーを中間層として共押出した非晶積層フィルム
を延伸した後に各層に剥離する方法(例えば特願昭49-1
04564号、特開昭61-31236号)や、スペーサーを使用し
ない方法(特開平6-305016号)などが知られている。2. Description of the Related Art As a method for producing a plurality of films made of a thermoplastic resin all at once for the purpose of improving productivity, a method of stretching an amorphous laminated film coextruded with a peeling spacer as an intermediate layer and then peeling the film into each layer. (For example, Japanese Patent Application No. 49-1
No. 04564, JP-A-61-31236) and a method using no spacer (JP-A-6-305016) are known.
【0003】しかし、特開昭61-31236号の方法ではフィ
ルムエッジの回収が困難である、特願昭49-104564号の
方法では厚み斑のコントロールが困難である、また特開
平6-305016号の方法では複数のフィルムを別々のダイと
冷却ドラムを用いて製造し、かつ結晶化度を制御すると
いう設備上と運転上の煩雑さがある等の問題を抱えてい
る。However, it is difficult to recover the film edge by the method disclosed in Japanese Patent Application Laid-Open No. 61-31236, it is difficult to control the thickness unevenness by the method disclosed in Japanese Patent Application No. 49-104564. However, the method (1) has a problem in that a plurality of films are manufactured using separate dies and cooling drums, and the degree of crystallinity is controlled.
【0004】[0004]
【発明が解決しようとしている課題】本発明の目的は、
上記の従来技術の問題を解消し、厚み斑がなく、また薄
膜特に易接着薄膜を塗設したフィルムを巻き取っる場合
薄膜層同士のブロッキング等のトラブルを回避する熱可
塑性フィルムを2つ以上同時に製造する方法を提供する
ことにある。SUMMARY OF THE INVENTION The object of the present invention is to
In order to solve the above-mentioned problems of the prior art, there is no unevenness of thickness, and when winding a film coated with a thin film, particularly an easily adhesive thin film, two or more thermoplastic films are simultaneously used to avoid troubles such as blocking between thin film layers. It is to provide a manufacturing method.
【0005】[0005]
【課題を解決するための手段】本発明の目的は、本発明
によれば、相互に非相溶の熱可塑性樹脂を積層押出し急
冷して非晶積層フィルムとし、これを1軸延伸もしくは
2軸延伸し、さらに熱固定して引き取るに際し、延伸、
熱固定後の延伸積層フィルムを1対のロール間隙で実質
的に剥離点を固定して各層同時に剥離し、その後各単層
フィルムを個別のワインダーで巻き取ることを特徴とす
る熱可塑性フィルムの製造方法によって達成される。According to the present invention, it is an object of the present invention to laminate and extrude mutually incompatible thermoplastic resins and rapidly cool them to form an amorphous laminated film, which is uniaxially stretched or biaxially stretched. Stretching, heat-fixing and taking over, stretching,
Producing a thermoplastic film, wherein the stretched laminated film after heat setting is substantially fixed at a peeling point between a pair of rolls, and the respective layers are simultaneously peeled off, and then each single-layer film is wound up by an individual winder. Achieved by the method.
【0006】本発明においては、製品フィルム層とこれ
とは非相溶の樹脂層(剥離用スペーサー)とが交互に積
層された構造をとるように、相互に非相溶の熱可塑性樹
脂を共押出し急冷して非晶積層フィルムとし、次いでこ
れを延伸、熱固定処理するが、共押出ダイは各層の幅方
向の厚み調整が独立して行えるものが好ましい。さら
に、各層の溶融熱可塑性樹脂の押出し量は独立に制御で
きるようにするのが好ましい。また、延伸、熱固定を行
った延伸積層フィルムを1対のロールのニップ点、もし
くは1対のロールの比較的狭い間隙点において複数のフ
ィルムをほぼ同時に剥離し、剥離後の各単層フィルムの
幅方向厚みプロファイルを計測し、目標厚みの偏差に対
し、前記の厚み制御ダイにフィードバックすることによ
り均一な厚みとするのが好ましい。In the present invention, mutually incompatible thermoplastic resins are co-exposed so that a product film layer and an incompatible resin layer (separation spacer) are alternately laminated. The film is extruded and quenched to form an amorphous laminated film, which is then stretched and heat-set. Preferably, the co-extrusion die is capable of independently controlling the thickness of each layer in the width direction. Further, it is preferable that the extrusion amount of the molten thermoplastic resin in each layer can be controlled independently. In addition, the stretched laminated film that has been stretched and heat-set is peeled at a nip point of a pair of rolls or at a relatively narrow gap point of a pair of rolls at substantially the same time and a plurality of films are peeled off. It is preferable to measure the thickness profile in the width direction and feed back the deviation of the target thickness to the above-mentioned thickness control die to make the thickness uniform.
【0007】本発明においては、また、延伸、熱固定後
に各層を剥離するが、これによって製品フィルムのエッ
ジ回収が従来通り可能となり、またスペーサーとして押
出されたフィルムも全量回収でき、有効に再利用可能と
なる。更に本発明においては、1枚の剥離用スペーサー
の両表層に製品フィルムを押出す3層フィルムの場合、
未延伸積層フィルムまたは1軸延伸積層フィルムの両面
に易接着インラインコートを行い巻き取ることも好まし
い。一般的には両面に易接着層を有するフィルムを巻き
取ると、易接着層同士が貼り付く現象が見られるが、本
発明では上記のように単層フィルムに剥離した後巻き取
られる為、易接着層と非易接着層が交互に配置すること
になり、貼り付き現象が無くなると共に、2つの製品フ
ィルムに同時に片面塗工処理が行われ、大幅な生産性の
向上が実現できる。[0007] In the present invention, each layer is peeled after stretching and heat setting. This makes it possible to recover the edge of the product film as before, and the entire amount of the film extruded as a spacer can be recovered, so that it can be effectively reused. It becomes possible. Furthermore, in the present invention, in the case of a three-layer film in which a product film is extruded on both surface layers of one release spacer,
It is also preferable that the unstretched laminated film or the uniaxially stretched laminated film is subjected to easy adhesion in-line coating on both sides and wound. Generally, when a film having an easy-adhesion layer on both sides is wound up, a phenomenon in which the easy-adhesion layers adhere to each other is observed, but in the present invention, since the film is peeled off as a single-layer film as described above, it is easily wound. Since the adhesive layers and the non-easily adhesive layers are alternately arranged, the sticking phenomenon is eliminated and the two product films are simultaneously subjected to one-side coating, so that a significant improvement in productivity can be realized.
【0008】本発明において、熱可塑性樹脂としてはシ
ートまたはフィルムに押出成形できるものであればいか
なる樹脂でもよく、例えばポリエチレン、ポリプロピレ
ンのようなポリオレフィン、ポリ塩化ビニール、ポリ塩
化ビニリデンのような含塩素ポリマー、ナイロン6、ナ
イロン66のようなポリアミド、ポリエチレンテレフタ
レート、ポリエチレンナフタレートのようなポリエステ
ル、ポリカーボネート、ポリエーテルケトン、ポリエー
テルエーテルケトンのようなポリエーテル樹脂,ポリス
ルフォンサルフィドのようなスルフォン樹脂等を挙げる
ことができる。また、これらの樹脂と組み合せる非相溶
樹脂としては、ポリオレフィンに対する非相溶樹脂とし
てはポリアミド、ポリエステル、ポリエーテル,ポリス
ルフォンが好ましく、含塩素ポリマーに対してはポリア
ミド、ポリエステル、ポリエーテル,ポリスルフォンが
好ましく、ポリアミドに対してはポリオレフィン、ポリ
エステル、ポリエーテル,ポリスルフォンが好ましく、
ポリエステルに対してはポリオレフィン、ポリアミド、
ポリエーテル,ポリスルフォンが好ましく、ポリエーテ
ル樹脂には、ポリオレフィン、ポリアミド、ポリエステ
ル,ポリスルフォンが好ましい。これらの中ポリエステ
ルとポリオレフィンの組合せが特に好ましいこれらの組
合せによる積層フィルムは、共押出工程およびこれに引
き続く1軸延伸,2軸延伸の工程内では剥離せずに密着
していること,そして単独のフィルムとして使用するた
めの剥離工程では簡単に剥離されることが望ましい。好
ましい剥離張力は0.1g/cm以上 50g/cm以
下である。In the present invention, the thermoplastic resin may be any resin as long as it can be extruded into a sheet or a film. For example, polyolefins such as polyethylene and polypropylene, and chlorine-containing polymers such as polyvinyl chloride and polyvinylidene chloride. Polyamide such as nylon 6, nylon 66, polyester such as polyethylene terephthalate, polyethylene naphthalate, polyether resin such as polycarbonate, polyetherketone, polyetheretherketone, and sulfone resin such as polysulfone sulfide. Can be mentioned. As the incompatible resin to be combined with these resins, polyamide, polyester, polyether, and polysulfone are preferable as the incompatible resin for polyolefin, and for the chlorine-containing polymer, polyamide, polyester, polyether, and polysulfone are preferable. Sulfone is preferred, and for polyamide, polyolefin, polyester, polyether and polysulfone are preferred,
For polyester, polyolefin, polyamide,
Polyether and polysulfone are preferable, and polyolefin, polyamide, polyester and polysulfone are preferable as the polyether resin. The laminated film of these combinations in which a combination of a polyester and a polyolefin is particularly preferable is that the film is adhered without peeling in the co-extrusion step and the subsequent uniaxial stretching and biaxial stretching steps. It is desirable that the film be easily peeled in a peeling step for use as a film. The preferable peel tension is 0.1 g / cm or more and 50 g / cm or less.
【0009】本発明における延伸・熱固定後の剥離に
は,ある程度の高い密着力に抗して,破断や剥離帯電等
の静電気障害を生じない安定な方法が必要である。これ
には,各層の剥離点が幅方向に横一線に剥離されること
が好ましく,上記したように機械的に剥離点を固定する
押さえロールを用いること必要である。また,剥離後の
各層フィルムの引き取り張力は層間の密着力より若干高
いことが好ましい。この張力が低すぎる場合は、剥離点
が下流側に移動すると共に、幅方向で剥離点がずれてフ
ィルムの引き裂かれ現象につながり、好ましくない。剥
離張力が、フィルム相互の密着力より十分に高ければ前
記のロールニップ点で剥離点が固定されるが、薄いフィ
ルムでは、無闇に高い張力は切断の可能性もあり、高張
力が採れない場合がある。この場合には、密着力より若
干高い程度の剥離張力であっても剥離点が安定的に固定
されるよう、フィルム層間に加圧空気を剥離点に向けて
吹き込むことが好ましい。For the peeling after stretching and heat fixing in the present invention, a stable method is required which does not cause static electricity damage such as breakage or peeling electrification against a certain high adhesive force. For this purpose, it is preferable that the peeling points of the respective layers are peeled off in a horizontal line in the width direction, and it is necessary to use a press roll for mechanically fixing the peeling points as described above. Further, it is preferable that the take-up tension of each layer film after peeling is slightly higher than the adhesion between the layers. If the tension is too low, the peeling point moves downstream, and the peeling point shifts in the width direction, leading to a tearing phenomenon of the film, which is not preferable. If the peeling tension is sufficiently higher than the adhesion between the films, the peeling point is fixed at the roll nip point.However, in the case of a thin film, high tension may be cut indiscriminately. is there. In this case, it is preferable to blow pressurized air between the film layers toward the peeling point so that the peeling point is stably fixed even if the peeling tension is slightly higher than the adhesion force.
【0010】また高絶縁性の樹脂フィルムを剥離する場
合、一般的に剥離帯電が発生し、エレクトロレット等の
静電気障害が生じる。この解消策としては前記加圧空気
の吹き込みをイオン化空気とすることが有効であり、こ
れによって効果的に剥離帯電を除電出来る。[0010] When a highly insulating resin film is peeled off, peeling charging generally occurs, causing an electrostatic failure such as an electrolet. As a countermeasure for this, it is effective to blow the pressurized air with ionized air, thereby effectively removing the peeling charge.
【0011】以下、図面を用いて本発明をさらに説明す
る。図1は本発明の一つの実施態様を示す積層フィルム
の製造工程の側面図であり、図2はこの積層フィルムの
各層の幅方向厚みを調整しうる押出ダイの断面図であ
る。Hereinafter, the present invention will be further described with reference to the drawings. FIG. 1 is a side view of a manufacturing process of a laminated film showing one embodiment of the present invention, and FIG. 2 is a cross-sectional view of an extrusion die capable of adjusting the thickness in the width direction of each layer of the laminated film.
【0012】図1において,1は製品フィルムを押出す
押出機、2は第1フィルター、3、3’は各表層の吐出
量を制御する計量ポンプであり、このポンプで目標の製
品厚み(同厚みまたは異厚み)に調整することができ
る。なお、3、3’は、絞り弁で代替することも出来
る。4、4’は表層の第2フィルターを示す。5は剥離
フィルムの押出機、6は計量ポンプ、7はフィルターを
示す。8は押出ダイで、製品フィルムと剥離フィルムを
積層するとともに、各層の幅方向厚み制御が可能な機能
を有する。In FIG. 1, 1 is an extruder for extruding a product film, 2 is a first filter, and 3 and 3 'are metering pumps for controlling the discharge amount of each surface layer. (Thickness or different thickness). In addition, 3, 3 'can be replaced with a throttle valve. Reference numerals 4 and 4 ′ denote surface second filters. Reference numeral 5 denotes a release film extruder, 6 denotes a metering pump, and 7 denotes a filter. Reference numeral 8 denotes an extrusion die, which has a function of laminating a product film and a release film and controlling the thickness of each layer in the width direction.
【0013】押出しダイを図2にてより詳細に説明する
と、31は剥離用樹脂のマニホールドである。幅方向の
流量調整は、流動間隙32を形成する薄板をヒートボル
ト式熱伸縮アクチュエーター33により押し引きするこ
とにより行われ、これをダイ幅方向に複数設置し厚み調
整を行うことが出来る。33’は同様なヒートボルト式
アクチュエーターであり、33に相対してもしくは千鳥
状に配置される。The extrusion die will be described in more detail with reference to FIG. 2. Reference numeral 31 denotes a release resin manifold. The flow rate adjustment in the width direction is performed by pushing and pulling the thin plate forming the flow gap 32 by the heat bolt type thermal expansion / contraction actuator 33, and a plurality of the thin plates can be installed in the die width direction to adjust the thickness. Reference numeral 33 'denotes a similar heat bolt type actuator which is arranged opposite to or in a zigzag manner.
【0014】また製品フィルムとなる熱可塑性樹脂はマ
ニホールド35、35’に流れ、間隙36のギャップ調
整を前記の如くヒートボルトで行っても良く、または本
図の如く温度により樹脂粘度を変化させて流量を調整す
る場合は、間隙36、36’に近接したヒーター37、
37’をダイ幅方向に複数配置して調整することが出来
る。なお、溶融樹脂が層状に合流したのちの流路は短い
程好ましく、従って各層の合流点38から樹脂出口39
までの距離は極力短いことが好ましく、具体的には0mm
から20mm程度が好ましい。この距離が長くなると、各
層の調整効果が相互に干渉し合い、調整能力が低下する
ようになる。The thermoplastic resin as a product film flows to the manifolds 35 and 35 ', and the gap of the gap 36 may be adjusted by a heat bolt as described above, or by changing the resin viscosity according to the temperature as shown in FIG. When adjusting the flow rate, the heater 37 close to the gap 36, 36 ',
37 'can be adjusted by arranging a plurality of 37' in the die width direction. It is preferable that the flow path after the molten resin joins in layers is shorter, and therefore, the resin outlet 39 from the junction 38 of each layer is preferred.
Is preferably as short as possible, specifically 0 mm
From about 20 mm. When the distance is long, the adjustment effects of the respective layers interfere with each other, and the adjustment ability is reduced.
【0015】以下図1に戻って説明すると、積層フィル
ムは冷却ドラム9で非晶状態に近く急冷され、引き続き
縦延伸10、横延伸12、熱固定される。本例では縦延
伸後に積層フィルムの両面に11、11’に示すコーテ
ィングを行う例を示しているが、縦横同時2軸延伸の場
合は、延伸前の未延伸フィルムにコーティングを行って
も良い。延伸熱固定後の延伸積層フィルムはロール13
で冷却後、1対のロール14、14’により、押圧もし
くは僅かの間隙を有する状態で、表層フィルムAと中層
剥離フィルムB、及びもう一方の表層フィルムCに剥
離、分離される。この剥離張力はそれぞれに駆動ニップ
ロール15、16、17とロール14の周速度差により
付与すると同時に、後工程の巻取り、粉砕からの張力変
動をカットし安定な剥離を可能とする。また、積層フィ
ルムを剥離する際、一般的には強度の剥離帯電を生ずる
ことが多く、不規則な放電痕等の静電気障害を起こす。
この為、フィルムの剥離点に向けて、除電用イオン風を
ノズル18、18’により、それぞれの剥離点に吹き込
むことが好ましい。表層フィルムAはその後幅方向の厚
み分布を厚み計19(例えばβ線厚み計)により計測さ
れ、目的厚みの偏差に対応し制御装置29を経由し、ダ
イの制御子37’にフィードバックされ、均一なフィル
ムに調整することが出来る。フィルムAはエッジ20を
裁断した後、ワインダー21で巻き取られる。またスペ
ーサー用フィルムBは剥離した後、製品化せず回収する
ケースを示す。このフィルムは製品にならない為、厚み
均一性は製品レベル程の厳密性は必要ないが、延伸熱固
定時にスペーサーフィルムに大きな厚み偏差が有ると加
熱冷却過程で温度差を生じ、これに密着している製品フ
ィルムの温度分布も変化し、配向物性、結晶化度等の物
性不均一を来すことになる為、ある程度の厚み制御が必
要となる。本例では、光干渉膜厚計22を幅方向にスキ
ャン可能に設置し、測定された厚み偏差に応じて制御出
力をダイの中層の厚薄制御用ヒートボルト33、33’
に与え、幅方向の厚みプロファイル調整を行う。該スペ
ーサーフィルムは一旦巻き取っていも良いが、効率よく
回収再生する例として、本図の如く吸引エゼクター25
により、直接粉砕機へ、または再生造粒機等に搬送する
ことが好ましい。また該スペーサーフィルムが広幅の場
合は、全幅フィルムであると搬送し難い場合があり、適
宜幅方向に裁断し折り曲げもしくは束ねた後、搬送する
ことが好ましい。この為、本例に裁断用カッター23及
び絞りガイド24を例示する。もう一方の製品表層フィ
ルムCは、フィルムAと同様に厚み計26にて、計測し
偏差を図2のダイ制御ヒーター37により調整さる。フ
ィルムCは27のエッジトリム後、ワインダー28で巻
き取られる。Referring back to FIG. 1, the laminated film is rapidly cooled to a non-crystalline state by a cooling drum 9 and then longitudinally stretched 10, transversely stretched 12, and thermally fixed. In this example, an example is shown in which coatings 11 and 11 'are applied to both surfaces of the laminated film after longitudinal stretching, but in the case of simultaneous biaxial stretching in the vertical and horizontal directions, the unstretched film before stretching may be coated. The stretched laminated film after stretching heat setting is roll 13
After being cooled, the film is separated and separated into a surface film A, an intermediate release film B, and another surface film C by a pair of rolls 14 and 14 ′ while pressing or having a slight gap. This peeling tension is imparted by the peripheral speed difference between the drive nip rolls 15, 16, 17 and the roll 14, respectively, and at the same time, the fluctuation in the tension from winding and grinding in the post-process is cut to enable stable peeling. In addition, when the laminated film is peeled, generally, strong peeling charge is often generated, which causes electrostatic damage such as irregular discharge marks.
For this reason, it is preferable that the ion-exhausting ion wind is blown into the respective peeling points by the nozzles 18 and 18 'toward the film peeling points. The thickness distribution of the surface film A in the width direction is thereafter measured by a thickness gauge 19 (for example, a β-ray thickness gauge), and is fed back to the die controller 37 ′ via the control device 29 in accordance with the deviation of the target thickness, and is uniform. Can be adjusted to a suitable film. The film A is wound by a winder 21 after cutting the edge 20. In addition, a case is shown in which the spacer film B is recovered without being commercialized after peeling. Since this film does not become a product, the thickness uniformity does not need to be as strict as the product level.However, if there is a large thickness deviation in the spacer film during stretching heat setting, a temperature difference will occur in the heating and cooling process, and it will adhere to this. The temperature distribution of the product film also changes, resulting in non-uniform physical properties such as orientation physical properties and crystallinity, so that a certain degree of thickness control is required. In this example, the optical interference film thickness meter 22 is installed so as to be able to scan in the width direction, and the control output is changed according to the measured thickness deviation to the thickness of the middle layer of the die.
To adjust the thickness profile in the width direction. The spacer film may be once wound up, but as an example of efficiently collecting and regenerating, the suction ejector 25 shown in FIG.
, It is preferable to transport directly to a pulverizer or a regenerated granulator. When the spacer film is wide, it may be difficult to convey the film if it is a full-width film. It is preferable that the film is appropriately cut in the width direction, bent or bundled, and then conveyed. For this reason, the cutter 23 and the squeeze guide 24 are illustrated in this example. The other product surface film C is measured by the thickness gauge 26 in the same manner as the film A, and the deviation is adjusted by the die control heater 37 in FIG. The film C is wound up by a winder 28 after the edge trimming of 27.
【0016】図1では,3層積層の剥離の例を示した
が,例えば2つの剥離フィルムと3つの製品フィルムを
交互に挟んだ5層の積層フィルムを延伸熱固定し、単層
フィルムに剥離分離することも,本発明の一つの態様と
して有用である。FIG. 1 shows an example of peeling of a three-layer laminate. For example, a five-layer laminate film in which two release films and three product films are alternately sandwiched is stretched and heat-fixed, and peeled into a single-layer film. Separation is also useful as one embodiment of the present invention.
【0017】本発明によれば,このように複数の熱可塑
性フィルム一挙に製造することができ、更には複数の製
品フィルムを,厚み斑なく、また易接着塗布したフィル
ムを巻き取った場合にも、塗布層同士のブロッキング等
による欠陥を回避することができ、高品質なフィルムを
大幅な生産性を確保しながら製造することができる。According to the present invention, a plurality of thermoplastic films can be manufactured at once as described above. Further, even when a plurality of product films are rolled up without unevenness in thickness and easily applied and coated, In addition, it is possible to avoid defects due to blocking between coating layers and the like, and it is possible to produce a high-quality film while securing significant productivity.
【0018】本発明の特徴は,上述したようにまず、延
伸後にフィルムを剥離し巻き取ることにより大きな効果
が得られることである。次ぎに、製品フィルムを単層フ
ィルムとすることにより厚み測定が容易になり、各層厚
み分布が調整可能なダイと組み合わせることで、厚み偏
差の少ない製品フィルムを得ることが出来ることであ
る。さらに、フィルムエッジの回収が従来通り容易に行
うことができることである。更に本発明の大きな特徴
は、例えば剥離フィルムの両側に製品フィルムを押出し
て3層フィルムとなし、この未延伸もしくは1軸延伸フ
ィルムの両面に易接着コーティングを行うことにより、
剥離後の製品フィルムには片面コーティングではある
が、同時にコーティング処理が可能であり、大きな生産
性の向上が得られる。更には、一般的に易接着コート層
は、コート層同士が巻取り等により押圧された場合、相
互に接着しブロッキング現象を起こし易いという問題が
あるが、本発明の方法によれば、製品フィルムが巻取ら
れる際は、接着層と非接着層が相対する為、ブロッキン
グ現象もなく、高い生産性と、高品質の両立した生産シ
ステムを提供することが出来る。A feature of the present invention is that a great effect can be obtained by first peeling and winding the film after stretching as described above. Next, the thickness of the product film can be easily measured by forming the product film into a single-layer film, and a product film having a small thickness deviation can be obtained by combining with a die capable of adjusting the thickness distribution of each layer. Further, the film edge can be easily collected as before. Further, a major feature of the present invention is that, for example, a product film is extruded on both sides of a release film to form a three-layer film, and the unstretched or uniaxially stretched film is coated with easy-adhesion on both sides.
Although the product film after peeling is a one-sided coating, it can be coated at the same time, and a large improvement in productivity can be obtained. Further, generally, the easily adhesive coat layer has a problem that when the coat layers are pressed by winding or the like, they easily adhere to each other and cause a blocking phenomenon. However, according to the method of the present invention, the product film When is wound, the adhesive layer and the non-adhesive layer are opposed to each other, so that there is no blocking phenomenon, and a production system that is compatible with high productivity and high quality can be provided.
【0019】一方、製品とならない中間層の剥離フィル
ム(スペーサーフィルム)の処理法としては、そのまま
巻き取っても良いが、これらのフィルムは廃棄せずに回
収もしくは再生使用することが環境保全上好ましい。従
って、巻取らず直接粉砕もしくは造粒再生する工程に直
接搬送し回収することが好ましい。On the other hand, as a method for treating a release film (spacer film) of an intermediate layer which does not become a product, it may be wound up as it is, but it is preferable from the viewpoint of environmental conservation to collect or recycle these films without discarding them. . Therefore, it is preferable to directly convey and collect in a step of directly grinding or granulating and regenerating without winding.
【0020】[0020]
【実施例】以下、実施例によって本発明をさらに説明す
る。The present invention will be further described with reference to the following examples.
【0021】[実施例1]ポリエチレン−2,6−ナフ
タレート(PEN)を両表層とし、ポリプロピレン(P
P)を中間層とした3層フィルムを図2の3層ダイで共
押出し、急冷して非晶積層フィルムとした後、1軸方向
に110℃で3.6倍延伸し、これに水系エマルジョン
易接塗剤を両面にコーティングし、引き続き延伸温度1
30℃で横方向に4.7倍延伸し、さらに210℃で熱
固定し、5.5μm/3.5μm/5.5μmの厚み構
成の3層の薄膜塗設延伸積層フィルムを得た。これを図
1に示す延伸後の剥離装置により、表層PENの剥離張
力を1Kg/m、中層PPの剥離張力を0.5Kg/
m、イオン化加圧空気を風速15m/秒で吹き付ける条
件で分離して、破断や静電気障害もなく良好なPENフ
ィルムの製品ロールを得た。また中間層のポリプロピレ
ンフィルムは上記の熱固定温度では,無配向に近くなり
破断し易くなるが,剥離後のポリプロピレンフィルムの
引取り張力をニップロール16以降0.3Kg/mに下
げることにより,破断もなく安定した搬送が可能であ
り,エジェクターに吸引可能であった。Example 1 Polyethylene-2,6-naphthalate (PEN) was used for both surface layers, and polypropylene (P
A three-layer film having P) as an intermediate layer is co-extruded with a three-layer die shown in FIG. 2, quenched to form an amorphous laminated film, and then stretched 3.6-fold at 110 ° C. in one axis direction. Both sides are coated with an easy-coating agent, and the stretching temperature is 1
The film was stretched 4.7 times in the transverse direction at 30 ° C., and further heat-set at 210 ° C. to obtain a three-layer thin film-coated stretched laminated film having a thickness of 5.5 μm / 3.5 μm / 5.5 μm. The peeling tension of the surface layer PEN was 1 kg / m and the peeling tension of the middle layer PP was 0.5 kg / m.
m, and ionized pressurized air was separated under the condition of blowing at a wind speed of 15 m / sec to obtain a good product roll of a PEN film without breakage or static electricity damage. At the above-mentioned heat setting temperature, the polypropylene film of the intermediate layer becomes nearly non-oriented and easily breaks. However, by reducing the take-up tension of the polypropylene film after peeling to 0.3 Kg / m after the nip roll 16, breakage may occur. And stable transport was possible, and suction was possible with the ejector.
【0022】[比較例1]実施例1と同様の両面易接着
コートした2軸配向3層フィルムを、3枚に剥離するこ
となく巻き取ったところ、巻取ロール内で、各巻取層間
の表層フィルム同士が、部分接着しブロッキングを起こ
し、重大な品質欠陥となった。[Comparative Example 1] A biaxially oriented three-layer film coated with the same double-sided adhesive film as in Example 1 was wound up into three sheets without being peeled off. The films partially adhered and blocked, resulting in significant quality defects.
【0023】[0023]
【発明の効果】本発明によれば,複数の熱可塑性フィル
ムを一挙に製造することができ、更には複数のフィルム
を厚み斑なく、容易にエッジトリミングもでき、樹脂原
料のロスも少なく、かつ易接着塗布したフィルムを巻き
取った場合にも塗布剤同士のブロッキング等のトラブル
を回避することができ、高品質なフィルムを大幅な生産
性を確保しながら製造することができる。According to the present invention, a plurality of thermoplastic films can be manufactured at once, and furthermore, a plurality of films can be easily trimmed without unevenness in thickness, loss of resin material is small, and Troubles such as blocking between the coating agents can be avoided even when the film coated with the easy-to-adhesive film is wound up, and a high-quality film can be manufactured while securing significant productivity.
【図1】本発明の一つの実施態様を示すフィルム製造装
置の側面図である。FIG. 1 is a side view of a film manufacturing apparatus showing one embodiment of the present invention.
【図2】本発明の一つの実施態様を示す3層フィルムを
積層するダイの断面図である。FIG. 2 is a cross-sectional view of a die for laminating a three-layer film showing one embodiment of the present invention.
1:製品フィルムの押出機 2:第1フィルター 3:計量ポンプ 4:第2フィルター 5:スペーサーフィルムの押出機 6:計量ポンプ 7:フィルター 8:ダイ 9:冷却ドラム 10:縦延伸機 11:インラインコーター 12:横延伸機 13:冷却ロール 14:剥離ロール 15、16、17:剥離張力制御ロール 18:イオン風ノズル 19:厚み計 20:エッジトリムフィルム 21:ワインダー 22:光干渉厚み計 23:裁断刃 24:絞りガイド 25:吸引エジェクター 26:厚み計 27:エッジトリムフィルム 28:ワインダー 29:厚みコントローラー 31:剥離樹脂用マニホールド 32:厚み調整間隙 33:ヒートボルトアクチュエーター 35:製品用樹脂マニホールド 36:厚み調整間隙 37:厚み制御ヒーター 38:合流点 39:積層樹脂出口 1: Extruder for product film 2: First filter 3: Metering pump 4: Second filter 5: Extruder for spacer film 6: Metering pump 7: Filter 8: Die 9: Cooling drum 10: Vertical stretching machine 11: Inline Coater 12: Horizontal stretching machine 13: Cooling roll 14: Peeling roll 15, 16, 17: Peeling tension control roll 18: Ion wind nozzle 19: Thickness gauge 20: Edge trim film 21: Winder 22: Optical interference thickness gauge 23: Cutting Blade 24: Squeeze guide 25: Suction ejector 26: Thickness gauge 27: Edge trim film 28: Winder 29: Thickness controller 31: Release resin manifold 32: Thickness adjustment gap 33: Heat bolt actuator 35: Product resin manifold 36: Thickness Adjustment gap 37: Thickness control heater 3 : Confluence 39: laminated resin exit
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI B29D 7/00 B29D 7/00 // B29K 101:12 105:26 B29L 7:00 (72)発明者 新口 正博 神奈川県相模原市小山3丁目37番19号 帝 人株式会社相模原研究センター内──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification symbol FI B29D 7/00 B29D 7/00 // B29K 101: 12 105: 26 B29L 7:00 (72) Inventor Masahiro Niguchi Sagamihara, Kanagawa 3-37-19 Koyama-shi, Sagamihara Research Center, Teijin Limited
Claims (5)
層押出し急冷して非晶積層フィルムとし、これを1軸延
伸もしくは2軸延伸し、さらに熱固定して引き取るに際
し、延伸、熱固定後の延伸積層フィルムを1対のロール
間隙で実質的に剥離点を固定して各層同時に剥離し、そ
の後各単層フィルムを個別のワインダーで巻き取ること
を特徴とする熱可塑性フィルムの製造方法。1. An mutually incompatible thermoplastic resin is alternately laminated and extruded and rapidly cooled to form an amorphous laminated film, which is stretched uniaxially or biaxially, and then heat-fixed to draw it. A method for producing a thermoplastic film, wherein the stretched laminated film after fixing is peeled at the same time with a pair of rolls substantially fixing a peeling point and each layer is simultaneously peeled off, and then each single-layer film is wound up by an individual winder. .
押出し量と幅方向厚み調整機能を有する押出ダイにより
行い、延伸積層フィルムを単層に剥離した後、各単層フ
ィルムの幅方向厚み分布を計測し、目標値からの偏差に
対して各層の押出し量及び/又は各層の幅方向厚み調整
機能で厚み制御を行う請求項1記載の熱可塑性フィルム
の製造方法。2. Laminate extrusion of a thermoplastic resin is performed by an extrusion die having a function of adjusting the amount of extrusion and the thickness in the width direction independently of each layer, and after the stretched laminated film is peeled into a single layer, the thickness distribution in the width direction of each single-layer film. The method for producing a thermoplastic film according to claim 1, wherein the thickness is controlled by a function of adjusting the extrusion amount of each layer and / or the thickness in the width direction of each layer with respect to a deviation from a target value.
フィルムの両面に薄膜形成塗液を塗布し、その後乾燥、
延伸、熱固定処理を行って薄膜塗設延伸積層フィルムと
し、次いで該延伸積層フィルムを単層に剥離する請求項
1又は2記載の熱可塑性フィルムの製造方法。3. A thin film forming coating solution is applied to both sides of an amorphous laminated film or a uniaxially stretched laminated film, and then dried,
The method for producing a thermoplastic film according to claim 1 or 2, wherein the film is stretched and heat-set to form a thin film-coated stretched laminated film, and then the stretched laminated film is peeled into a single layer.
層フィルムの内、製品としない少なくとも1層の単層フ
ィルムをフィルム再押出用として回収する請求項1記載
の熱可塑性フィルムの製造方法。4. The method for producing a thermoplastic film according to claim 1, wherein at least one single-layer film, which is not a product, is recovered for re-extrusion of the plurality of single-layer films peeled from the stretched laminated film.
層フィルムの内、製品としない少なくとも1層の単層フ
ィルムを巻き取らず吸引搬送しもしくは引き取り粉砕
し、所望により造粒し、フィルム再押出用として回収す
る請求項1記載の熱可塑性フィルムの製造方法。5. A plurality of single-layer films peeled off from the stretched laminated film, wherein at least one single-layer film not formed as a product is sucked and conveyed or wound up without winding, granulated as required, and re-extruded. The method for producing a thermoplastic film according to claim 1, wherein the thermoplastic film is recovered for use.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8269752A JPH10113985A (en) | 1996-10-11 | 1996-10-11 | Manufacture of thermoplastic film |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8269752A JPH10113985A (en) | 1996-10-11 | 1996-10-11 | Manufacture of thermoplastic film |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10113985A true JPH10113985A (en) | 1998-05-06 |
Family
ID=17476670
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8269752A Pending JPH10113985A (en) | 1996-10-11 | 1996-10-11 | Manufacture of thermoplastic film |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH10113985A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112018200A (en) * | 2019-05-28 | 2020-12-01 | 汉能移动能源控股集团有限公司 | Preparation method of POE film |
CN114801140A (en) * | 2022-04-02 | 2022-07-29 | 万宗旺 | Film tube blowing equipment for producing degradable plastic bags and blowing process thereof |
CN119305159A (en) * | 2024-09-29 | 2025-01-14 | 佛山市盈博莱科技股份有限公司 | A dry single-pull diaphragm and preparation method thereof |
-
1996
- 1996-10-11 JP JP8269752A patent/JPH10113985A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112018200A (en) * | 2019-05-28 | 2020-12-01 | 汉能移动能源控股集团有限公司 | Preparation method of POE film |
CN114801140A (en) * | 2022-04-02 | 2022-07-29 | 万宗旺 | Film tube blowing equipment for producing degradable plastic bags and blowing process thereof |
CN119305159A (en) * | 2024-09-29 | 2025-01-14 | 佛山市盈博莱科技股份有限公司 | A dry single-pull diaphragm and preparation method thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2044117C (en) | Method of manufacturing thermoplastic sheet of film | |
EP0010895B1 (en) | Method of making laminates of thermoplastic polymers by a single-channel coextrusion process and melt injector block for use therein | |
EP2552666A2 (en) | Feedblock for making multilayered films | |
US5747107A (en) | Method of applying a hot melt coating | |
JP2000127227A (en) | Film extrusion device and manufacture of film | |
JPH10113985A (en) | Manufacture of thermoplastic film | |
US20100213632A1 (en) | Method and apparatus for manufacturing molded plate | |
EP1436136B1 (en) | Method for extrusion coating multiple webs | |
JP4857837B2 (en) | Propylene resin retardation film production method | |
CA2181056A1 (en) | Pressure sensitive adhesive tape | |
WO2014144205A2 (en) | Apparatus for manufacturing and processing pre-stretch films having strips of increased thickness | |
JP5062920B2 (en) | Coextrusion mold and its manifold system | |
JP2018058327A (en) | Method for manufacturing film | |
JP2023090816A (en) | Coating device, film manufacturing system, and film manufacturing method | |
JP3139271B2 (en) | Method for producing thermoplastic resin embossed sheet | |
CN114514106B (en) | Method for producing sealable biaxially oriented polyester-based films and film stretching device | |
JP3024458B2 (en) | Manufacturing method of thermoplastic resin laminate | |
JP2971391B2 (en) | Method and apparatus for manufacturing resin-coated metal sheet | |
JPH09314776A (en) | Separation of multilayer film | |
JP2002067141A (en) | Method for manufacturing sequentially biaxially stretched film | |
EP4214052A1 (en) | Knurled multilayer polyolefin films for use as antiadhesive interleaves, as well as process and technological line for manufacturing the same | |
JPH11207816A (en) | Production of thermoplastic resin film | |
JPS583809B2 (en) | Method for manufacturing multilayer resin body | |
JP2000117061A5 (en) | Manufacturing method of hollow fiber membrane module material | |
JP2006327011A (en) | Polymer film manufacturing method and roll of polymer film |