JPH0524814B2 - - Google Patents

Info

Publication number
JPH0524814B2
JPH0524814B2 JP61158835A JP15883586A JPH0524814B2 JP H0524814 B2 JPH0524814 B2 JP H0524814B2 JP 61158835 A JP61158835 A JP 61158835A JP 15883586 A JP15883586 A JP 15883586A JP H0524814 B2 JPH0524814 B2 JP H0524814B2
Authority
JP
Japan
Prior art keywords
heater
temperature
lip
die
resin
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 - Lifetime
Application number
JP61158835A
Other languages
Japanese (ja)
Other versions
JPS6315725A (en
Inventor
Sumio Goto
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 JP61158835A priority Critical patent/JPS6315725A/en
Publication of JPS6315725A publication Critical patent/JPS6315725A/en
Publication of JPH0524814B2 publication Critical patent/JPH0524814B2/ja
Granted 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
    • B29C48/03Extrusion 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
    • B29C48/07Flat, e.g. panels
    • B29C48/08Flat, e.g. panels flexible, e.g. films
    • 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
    • B29C2948/92009Measured parameter
    • B29C2948/92209Temperature
    • 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
    • B29C2948/92323Location or phase of measurement
    • B29C2948/92428Calibration, after-treatment, or cooling zone
    • 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
    • B29C2948/9258Velocity
    • B29C2948/926Flow or feed rate
    • 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
    • B29C2948/92857Extrusion unit
    • B29C2948/92904Die; Nozzle zone

Description

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

〔産業上の利用分野〕 本発明は、溶融した熱可塑性樹脂をダイから冷
却ロール面上に押出してフイルム類(本発明では
フイルムはもちろんのことシートも含めた意味で
用いる)を製造する方法において、偏肉の少ない
均質なフイルム類を安定して成形することのでき
る熱可塑性樹脂フイルム類の製造方法に関する。 〔従来の技術〕 従来より熱可塑性樹脂フイルムの製造方法とし
て、T−ダイより溶融した熱可塑性樹脂を膜状に
押出し、冷却ロールにより冷却固化させる方法が
知られている。 しかし、この方法は、ダイ巾方向の単位長さ当
りの溶融樹脂の流量に差があるため、フイルムの
巾方向に偏肉が発生し易い欠点があつた。 そこで、このフイルムの巾方向の偏肉を少なく
する方法として、チヨークバー、移動リツプ、フ
レキシブルリツプ(リツプ部を機械的にたわま
せ、リツプ開度の変更を行なう)を用いた方法が
知られている。 すなわち、フイルムの成形時にダイリツプ近傍
の樹脂流路のギヤツプを変更させることにより、
フイルムの偏肉を調整する方法であるが、この方
法は差動ネジ等で流路ギヤツプの変更を行なうた
め、言い換えればネジ等のピツチ及びあそびによ
り偏肉調整精度が決定されるため、その精度は充
分満足すべきものではなかつた。 また、別の公知技術として金属の熱膨脹により
機械的に樹脂流路のギヤツプを変更させる方法も
知られているが、これは金属の膨脹と収縮及びリ
ツプ部の歪みを利用しているので、偏肉調整精度
としては充分な効果が得られなかつた。 〔発明が解決しようとする問題点〕 本発明の目的は、上記の問題点を解決し高い偏
肉調整精度のもとで偏肉の少ない均質なフイルム
類を安定して製造することのできる熱可塑性樹脂
フイルム類の製造方法を提供することにある。 〔問題点を解決するための手段および作用〕 本発明は溶融した熱可塑性樹脂をダイから冷却
ロール面上に押出してフイルム類を製造する方法
において、 巾方向で異なる温度プロフアイルを設定可能な
ヒーターをダイのリツプ近傍に設置し、 前記ヒーターの少なくとも一部がダイの巾方向
に沿つて巾50mm以下の複数個の部分に分割され、 前記ヒーターが前記リツプ出口から200mm以内
の距離に配置され、かつ 前記リツプ出口近傍の樹脂温度プロフアイルを赤
外線温度センサーにより検出し、あらかじめ求め
ておいた目標温度プロフアイルと該樹脂温度プロ
フアイルの差を、前記ヒーターの設定温度プロフ
アイルの補正により解消することによつて、前記
リツプから押出される樹脂量を巾方向において均
一化することを特徴とする高度に均一な厚みの熱
可塑性樹脂フイルム類の製造方法に関する。 以下、図面を参照しながら本発明を詳しく説明
する。 第1図において、押出機(図示せず)で溶融混
練された熱可塑性樹脂はジヨイント1を通つてダ
イ2に流入し、ダイリツプ3からダイ外部へ押出
され、冷却ロール4,5を経てフイルム6として
引取られる。ダイ2にはダイ全体の温度を一定に
保つため、ヒーター8が取付けられており、加熱
温度は熱電対(図示せず)等で検出され、温調器
(図示せず)で調整される。7はダイリツプ調整
ボルトで、これを回転することにより樹脂量を調
整し、フイルムの偏肉を粗調整する。さらにダイ
リツプ3近傍には第2図にも明らかなように、巾
方向に偏肉調整用のヒーター9が設けられ、該ヒ
ーター9はコントローラ11と電気的に接続さ
れ、このコントローラ11にはダイリツプ3近傍
に配設した、赤外線温度センサー10が電気的に
接続されている。 ヒーター9は熱源として電熱方式を採用し、図
示のように複数個(図面ではたとえば18ヶ)のブ
ロツクに分割されていることが好ましく、各ブロ
ツク毎に温度設定が可能である。 コントローラ11には、ヒーター9の各ブロツ
ク毎に目標温度プロフアイルがインプツトされ
る。コントローラ11は上記目標温度に従つてヒ
ーター9に通電し、温度の設定を行なう。その通
電方法としてはトライアツク等で行なうことが可
能であり、電圧値または電流値を変化せしめヒー
ター9の発熱量を制御する方法とか、ヒーター9
への通電をON,OFFして発熱量を制御する方法
などが採用される。ヒーター9の温度設定が行な
われた後、リツプ3から押出される溶融樹脂の温
度は、ヒーター9の各ブロツクの目標温度に従つ
て変化する。しかし、外気温や各ブロツクの相互
の干渉等により溶融樹脂温度プロフアイルは目標
温度プロフアイルと異なる場合が多いから、ある
時間が経過したのちにコントローラ11は目標プ
ロフアイルとの差を補正するため、ヒーター9に
対して補正した温度の設定する。以上の動作の繰
り返しにより、溶融樹脂温度は目標プロフアイル
に近くなり、精度の良い温度制御が可能となる。
たとえばフイルムの厚みが一部で薄いような場合
は、該当するヒーター9の温度設定を上昇させて
温度を高めてやる。そうすると、その近傍のダイ
リツプ3内の樹脂流量が増加し、フイルムの厚み
が大きくなり、フイルムの巾方向の偏肉が減少
し、厚薄差の少ないフイルムが得られる。 本発明において、偏肉調整用のヒーター9は図
面ではダイ巾全体に設けられているが、フイルム
の耳部は実質的に製品として用いられないため、
ダイ巾の中間部のみ設けてもよい。 ヒーター9はブロツク巾50mm以下とすることが
必要で、とくに5mm以上、30mm以下でそれぞれ温
度調整可能な構造とし、かつ独立の温度となるよ
う複数個のブロツクに分割したものが好ましい。 ヒーター9のブロツク巾が50mmを越えた場合
は、フイルムの偏肉調整精度が十分でない。 ヒーター9の構造は電熱を熱源とするが、各ブ
ロツク内で均一な温度とするため、構造材として
は熱伝導性の良い金属、とくにアルミニウムが好
ましい。ヒーター9の代表例としては、熱伝導性
の良好なアルミニウムがヒーターの回りを囲んで
いる公知のアルミニウム鋳込ヒーターがあげられ
る。 ダイリツプ3からどの距離にヒーター9を設置
するかもフイルム偏肉調整精度に影響を及ぼす因
子となるもので、その距離が遠い場合は偏肉調整
精度が低下する。本発明ではダイリツプ3からヒ
ーター9までの距離は200mm以下、好ましくは150
mm以下、さらに好ましくは5mm以上100mmである。
ヒーター9はたとえ一部でも上記範囲に入つてい
れば構わないので、ヒーター9の他端は200mmを
越えても本発明に含まれる。因みに公知技術の中
にダイリツプ部にリツプヒーターやカートリツジ
ヒーターを設けるものがあるが、これはリツプ温
度を一定化しようとるものであり、本発明とは本
質的に全く異なるものである。 また本発明で用いられる熱可塑性樹脂とは、公
知のフイルム類の成形で知られているものならば
全て使用可能であり、代表例を挙げると、ポリエ
チレン、ポリプロピレンなどのポリオレフイン、
ポリエチレンテレフタレートのようなポリエステ
ル、ポリスチレンのようなポリビニル、ナイロン
66又はナイロン6のようなポリアミド、ポリカー
ボネートなどがある。 なお、本発明で用いられるダイ2は、従来の偏
肉調整方法で用いるチヨークバー、移動リツプ、
フレキシブルリツプ等を併用してもよく、併用し
た場合は粗調整を従来方法で行ない、微調整を本
発明方法で行なうことが望ましい。 〔実施例〕 以下、実施例をあげて本発明をさらに詳細に説
明する。 実施例1〜4および比較例1〜3 第1図に示す工程に従つて、下記に示す条件下
にポリプロピレンおよび低密度ポリエチレンのフ
イルムを成形した。なお、ダイ2のベースは実施
例、比較例ともにフレキシブルタイプで、リツプ
巾1500mm、リツプギヤツプ0.5mmで、実施例で用
いた温度センサー10には赤外非接触温度計を、
またヒーター9は電熱式のアルミニウム鋳込ヒー
ターを用いた。 実施例 1 成形条件:押出機温度180℃〜240℃、ジヨイント
温度240℃、ダイス温度240℃、樹脂温
度プロフアイル240+4 -0℃ 実施例 2 実施例1とヒーター9の分割数が異
なる他は同一の成形条件 比較例1 成形条件:押出機温度180℃〜240℃、ジヨイント
温度240℃、ダイス温度240℃ 実施例 3および4 成形条件:押出機温度180℃〜200℃、ジヨイント
温度200℃、ダイス温度200℃、樹脂温
度プロフアイル 200℃+4 -0℃ 比較例 2 成形条件:押出機温度180℃〜200℃、ジヨイント
温度200℃、ダイス温度200℃ 比較例 3 成形条件:押出機温度180℃〜200℃、ジヨイント
温度200℃、ダイス温度200℃、リツプ
ヒーター204℃
[Industrial Field of Application] The present invention relates to a method for manufacturing films (in the present invention, the meaning includes not only films but also sheets) by extruding a molten thermoplastic resin from a die onto the surface of a cooling roll. The present invention relates to a method for producing thermoplastic resin films that can stably form homogeneous films with less uneven thickness. [Prior Art] As a conventional method for producing a thermoplastic resin film, a method has been known in which a molten thermoplastic resin is extruded into a film through a T-die, and the extruded film is cooled and solidified using a cooling roll. However, this method has the disadvantage that uneven thickness tends to occur in the width direction of the film because there is a difference in the flow rate of the molten resin per unit length in the width direction of the die. Therefore, methods using a tie yoke bar, a movable lip, and a flexible lip (mechanically bending the lip part to change the opening degree of the lip) are known as methods for reducing the thickness unevenness in the width direction of the film. ing. That is, by changing the gap of the resin flow path near the die lip during film molding,
This is a method to adjust the uneven thickness of the film, but since this method changes the channel gap using a differential screw, etc., in other words, the accuracy of adjusting the uneven thickness is determined by the pitch and play of the screw, etc. was not completely satisfactory. Another known technique is to mechanically change the gap of the resin flow path by thermal expansion of the metal, but this method utilizes the expansion and contraction of the metal and the distortion of the lip, so it is not biased. A sufficient effect could not be obtained in terms of meat adjustment accuracy. [Problems to be Solved by the Invention] It is an object of the present invention to solve the above problems and to provide a heat treatment method that can stably produce homogeneous films with little thickness unevenness with high thickness unevenness adjustment accuracy. An object of the present invention is to provide a method for producing plastic resin films. [Means and effects for solving the problems] The present invention provides a method for manufacturing films by extruding a molten thermoplastic resin from a die onto a cooling roll surface, and provides a heater capable of setting different temperature profiles in the width direction. is installed near the lip of the die, at least a part of the heater is divided into a plurality of parts each having a width of 50 mm or less along the width direction of the die, and the heater is disposed at a distance of within 200 mm from the lip exit, and detecting a resin temperature profile near the lip outlet with an infrared temperature sensor, and eliminating the difference between a predetermined target temperature profile and the resin temperature profile by correcting the set temperature profile of the heater. The present invention relates to a method for producing thermoplastic resin films having highly uniform thickness, characterized in that the amount of resin extruded from the lip is made uniform in the width direction. Hereinafter, the present invention will be explained in detail with reference to the drawings. In FIG. 1, a thermoplastic resin melt-kneaded in an extruder (not shown) flows into a die 2 through a joint 1, is extruded from a die lip 3 to the outside of the die, passes through cooling rolls 4 and 5, and forms a film 6. It will be taken over as. A heater 8 is attached to the die 2 in order to keep the temperature of the entire die constant, and the heating temperature is detected by a thermocouple (not shown) or the like and adjusted by a temperature regulator (not shown). Reference numeral 7 is a die lip adjustment bolt, and by rotating this bolt, the amount of resin is adjusted, and uneven thickness of the film is roughly adjusted. Furthermore, as is clear from FIG. 2, near the die lip 3, a heater 9 is provided for adjusting the thickness unevenness in the width direction, and the heater 9 is electrically connected to a controller 11. An infrared temperature sensor 10 placed nearby is electrically connected. The heater 9 uses an electric heating system as a heat source, and is preferably divided into a plurality of blocks (for example, 18 blocks in the drawing) as shown, and the temperature can be set for each block. A target temperature profile is input to the controller 11 for each block of the heater 9. The controller 11 energizes the heater 9 in accordance with the target temperature to set the temperature. The energization method can be carried out by a tri-ac or the like, and a method of controlling the amount of heat generated by the heater 9 by changing the voltage value or current value, or a method of controlling the amount of heat generated by the heater 9.
Methods such as controlling the amount of heat generated by turning the power on and off are adopted. After the temperature of the heater 9 is set, the temperature of the molten resin extruded from the lip 3 changes according to the target temperature of each block of the heater 9. However, the molten resin temperature profile often differs from the target temperature profile due to the outside temperature and mutual interference between blocks, so after a certain period of time the controller 11 corrects the difference with the target profile. , and set the corrected temperature for the heater 9. By repeating the above operations, the temperature of the molten resin approaches the target profile, making it possible to control the temperature with high precision.
For example, if the thickness of the film is thin in some parts, the temperature setting of the corresponding heater 9 is increased to raise the temperature. Then, the flow rate of resin in the die lip 3 in the vicinity increases, the thickness of the film increases, the thickness deviation in the width direction of the film decreases, and a film with less difference in thickness can be obtained. In the present invention, the heater 9 for adjusting thickness unevenness is provided over the entire die width in the drawing, but since the edge of the film is not substantially used as a product,
It may be provided only in the middle part of the die width. It is necessary that the heater 9 has a block width of 50 mm or less, and it is particularly preferable that the heater 9 has a structure in which the temperature can be adjusted at 5 mm or more and 30 mm or less, and is divided into a plurality of blocks so that the temperature can be controlled independently. If the block width of the heater 9 exceeds 50 mm, the film thickness unevenness adjustment accuracy is not sufficient. The structure of the heater 9 uses electric heat as a heat source, and in order to maintain a uniform temperature within each block, the structural material is preferably a metal with good thermal conductivity, especially aluminum. A typical example of the heater 9 is a known aluminum cast heater in which the heater is surrounded by aluminum having good thermal conductivity. The distance at which the heater 9 is installed from the die lip 3 is also a factor that affects the accuracy of adjusting the thickness unevenness of the film, and if the distance is long, the accuracy of adjusting the thickness unevenness decreases. In the present invention, the distance from the die lip 3 to the heater 9 is 200 mm or less, preferably 150 mm or less.
mm or less, more preferably 5 mm or more and 100 mm.
It does not matter if even a portion of the heater 9 falls within the above range, so even if the other end of the heater 9 exceeds 200 mm, it is included in the present invention. Incidentally, there is a known technique in which a lip heater or a cartridge heater is provided in the die lip portion, but this is intended to keep the lip temperature constant, and is essentially completely different from the present invention. Furthermore, the thermoplastic resin used in the present invention can be any of those known for molding films, and typical examples include polyolefins such as polyethylene and polypropylene;
Polyester like polyethylene terephthalate, polyvinyl like polystyrene, nylon
Examples include polyamides such as 66 or nylon 6, and polycarbonates. Note that the die 2 used in the present invention is a die 2 used in the conventional uneven thickness adjustment method, such as a die yoke bar, a moving lip,
A flexible lip or the like may be used in combination, and when used in combination, it is desirable to perform coarse adjustment using the conventional method and fine adjustment using the method of the present invention. [Example] Hereinafter, the present invention will be explained in more detail with reference to Examples. Examples 1 to 4 and Comparative Examples 1 to 3 Polypropylene and low density polyethylene films were molded according to the steps shown in FIG. 1 under the conditions shown below. The base of the die 2 is a flexible type in both the example and the comparative example, with a lip width of 1500 mm and a lip gap of 0.5 mm, and the temperature sensor 10 used in the example is an infrared non-contact thermometer.
Further, as the heater 9, an electric type cast aluminum heater was used. Example 1 Molding conditions: extruder temperature 180°C to 240°C, joint temperature 240°C, die temperature 240°C, resin temperature profile 240 +4 -0 °C Example 2 The number of divisions of the heater 9 is different from Example 1. Comparative Example 1 under the same molding conditions Molding conditions: Extruder temperature 180°C to 240°C, joint temperature 240°C, die temperature 240°C Examples 3 and 4 Molding conditions: Extruder temperature 180°C to 200°C, joint temperature 200°C , die temperature 200℃, resin temperature profile 200℃ +4 -0 ℃ Comparative example 2 Molding conditions: Extruder temperature 180℃ to 200℃, joint temperature 200℃, die temperature 200℃ Comparative example 3 Molding conditions: Extruder temperature 180℃~200℃, joint temperature 200℃, die temperature 200℃, lip heater 204℃

【表】【table】

〔発明の効果〕〔Effect of the invention〕

本発明は以上で明らかな如く、溶融した熱可塑
性樹脂をダイから冷却面上に押出してフイルム類
を製造する際、ダイのリツプ近傍に巾方向で異な
る温度プロフアイルが設定可能なヒーターを設置
し、かつ上記リツプ出口近傍の樹脂温度プロフア
イルを検出する温度センサーを用い、上記リツプ
から押出される樹脂量を巾方向で調整するように
したので、高い偏肉調整精度の下で偏肉の少ない
フイルム類を安定して供給することができる。こ
うして成形されたフイルム類は後工定たとえばラ
ミネートやコーテイング法に適用した際、高い商
品価値を発揮することができる。
As is clear from the above, when manufacturing films by extruding molten thermoplastic resin from a die onto a cooling surface, the present invention installs a heater that can set different temperature profiles in the width direction near the lip of the die. In addition, the amount of resin extruded from the lip is adjusted in the width direction using a temperature sensor that detects the resin temperature profile near the exit of the lip, resulting in less uneven thickness with high thickness adjustment accuracy. Films can be stably supplied. Films formed in this manner can exhibit high commercial value when applied to post-processing processes such as lamination and coating methods.

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

第1図は本発明の一実施例を用いられる熱可塑
性樹脂フイルムの製造装置を示す構成図、第2図
は同装置のダイ部分の構成図である。 2…ダイ、3…ダイリツプ、4,5…冷却ロー
ル、8…ヒーター、9…偏肉調整用のヒーター、
10…温度センサー、11…コントローラ。
FIG. 1 is a block diagram showing a thermoplastic resin film manufacturing apparatus using an embodiment of the present invention, and FIG. 2 is a block diagram of a die portion of the same apparatus. 2...Die, 3...Die lip, 4, 5...Cooling roll, 8...Heater, 9...Heater for adjusting uneven thickness,
10...Temperature sensor, 11...Controller.

Claims (1)

【特許請求の範囲】 1 溶融した熱可塑性樹脂をダイから冷却ロール
面上に押出してフイルム類を製造する方法におい
て、 巾方向で異なる温度プロフアイルを設定可能な
ヒーターをダイのリツプ近傍に設置し、 前記ヒーターの少なくとも一部がダイの巾方向
に沿つて巾50mm以下の複数個の部分に分割され、 前記ヒーターが前記リツプ出口から200mm以内
の距離に配置され、かつ 前記リツプ出口近傍の樹脂温度プロフアイルを
赤外線温度センサーにより検出し、あらかじめ求
めておいた目標温度プロフアイルと該樹脂温度プ
ロフアイルの差を、前記ヒーターの設定温度プロ
フアイルの補正により解消することによつて、前
記リツプから押出される樹脂量を巾方向において
均一化することを特徴とする高度に均一な厚みの
熱可塑性樹脂フイルム類の製造方法。 2 前記ヒーターの熱伝導体としてアルミニウム
を用いることを特徴とする請求項1に記載の高度
に均一な厚みの熱可塑性樹脂フイルム類の製造方
法。
[Claims] 1. In a method for manufacturing films by extruding molten thermoplastic resin from a die onto the surface of a cooling roll, a heater capable of setting different temperature profiles in the width direction is installed near the lip of the die. , at least a portion of the heater is divided into a plurality of parts each having a width of 50 mm or less along the width direction of the die, the heater is disposed at a distance of within 200 mm from the lip exit, and the temperature of the resin near the lip exit is The profile is detected by an infrared temperature sensor, and the difference between a predetermined target temperature profile and the resin temperature profile is corrected by correcting the set temperature profile of the heater, thereby extruding from the lip. A method for producing thermoplastic resin films having highly uniform thickness, characterized by making the amount of resin applied uniform in the width direction. 2. The method for producing thermoplastic resin films having a highly uniform thickness according to claim 1, wherein aluminum is used as a heat conductor of the heater.
JP61158835A 1986-07-08 1986-07-08 Manufacture of thermoplastic resin film Granted JPS6315725A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61158835A JPS6315725A (en) 1986-07-08 1986-07-08 Manufacture of thermoplastic resin film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61158835A JPS6315725A (en) 1986-07-08 1986-07-08 Manufacture of thermoplastic resin film

Publications (2)

Publication Number Publication Date
JPS6315725A JPS6315725A (en) 1988-01-22
JPH0524814B2 true JPH0524814B2 (en) 1993-04-09

Family

ID=15680432

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61158835A Granted JPS6315725A (en) 1986-07-08 1986-07-08 Manufacture of thermoplastic resin film

Country Status (1)

Country Link
JP (1) JPS6315725A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ATE441512T1 (en) * 2004-05-18 2009-09-15 Betacontrol Gmbh & Co Kg Mess METHOD AND DEVICE FOR PRODUCING FLAT WEB PRODUCTS
JP4777694B2 (en) * 2005-06-09 2011-09-21 富士フイルム株式会社 Thermoplastic film and method for producing the same

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5295768A (en) * 1976-02-09 1977-08-11 Mitsubishi Plastics Ind Method of extrusion molding thermoplastic synthetic resin film
JPS56135028A (en) * 1980-02-21 1981-10-22 Windmoeller & Hoelscher Method of controlling thickness of flat film manufactured by flat film extruding device
JPS6176337A (en) * 1984-09-25 1986-04-18 Mitsubishi Heavy Ind Ltd Molten resin extruder

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5295768A (en) * 1976-02-09 1977-08-11 Mitsubishi Plastics Ind Method of extrusion molding thermoplastic synthetic resin film
JPS56135028A (en) * 1980-02-21 1981-10-22 Windmoeller & Hoelscher Method of controlling thickness of flat film manufactured by flat film extruding device
JPS6176337A (en) * 1984-09-25 1986-04-18 Mitsubishi Heavy Ind Ltd Molten resin extruder

Also Published As

Publication number Publication date
JPS6315725A (en) 1988-01-22

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