JPS62246713A - Controlling film thickness in apparatus for manufacturing synthetic resin film - Google Patents

Controlling film thickness in apparatus for manufacturing synthetic resin film

Info

Publication number
JPS62246713A
JPS62246713A JP61090760A JP9076086A JPS62246713A JP S62246713 A JPS62246713 A JP S62246713A JP 61090760 A JP61090760 A JP 61090760A JP 9076086 A JP9076086 A JP 9076086A JP S62246713 A JPS62246713 A JP S62246713A
Authority
JP
Japan
Prior art keywords
extrusion
take
film
calculated
synthetic 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.)
Pending
Application number
JP61090760A
Other languages
Japanese (ja)
Inventor
Toshio Ueda
敏夫 上田
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.)
MURAKAMI KOGYO KK
Murakami Kogyo Co Ltd
Original Assignee
MURAKAMI KOGYO KK
Murakami Kogyo Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by MURAKAMI KOGYO KK, Murakami Kogyo Co Ltd filed Critical MURAKAMI KOGYO KK
Priority to JP61090760A priority Critical patent/JPS62246713A/en
Publication of JPS62246713A publication Critical patent/JPS62246713A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B29C48/10Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/285Feeding the extrusion material to the extruder
    • B29C48/29Feeding the extrusion material to the extruder in liquid form
    • 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
    • B29C2948/92085Velocity
    • B29C2948/92104Flow 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
    • B29C2948/9258Velocity
    • 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
    • B29C2948/92609Dimensions
    • B29C2948/92628Width or height
    • 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
    • B29C2948/92819Location or phase of control
    • B29C2948/92933Conveying, transporting or storage of articles

Abstract

PURPOSE:To prepare a film of a desired thickness, by measuring an extruded quantity per unit hour from an extruder, comparing this measured value with a preset value and adjusting thereby a rotating speed of a take-up roller of the film. CONSTITUTION:Width W and a thickness t of a required film and a density rhoof a material are input in a micro computer M is advance. On the other hand, photoelectric material detecting device 17, 18 are connected with the micro computer M and a consuming hour T for a specified vol. of a resin material is detected by a detecting means D from the acting interval of the photoelectric material detecting device 17. An extrusion output per unit hour in an extrusion cylinder 3 is calculated by means of a calculating device O from the consuming hour T and a vol. 12 of an apparatus 12 for supplying the material constantly. By comparing this calculated extrusion output with the product of the desired thickness t and width w having been input in advance and calculating a take-up quantity per unit hour corresponding to the calculated extruded quantity, a rotating speed of a take-up roller 4 is controlled.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、例えばインフレーシaン法やTダイ法等、溶
融合成樹脂を押出機から押出すことにより合成樹脂フィ
ルムを形成するものにおいて、一定厚のフィルムを得る
ための方法に関する。
Detailed Description of the Invention (Field of Industrial Application) The present invention is applicable to methods such as the inflatable method and the T-die method in which a synthetic resin film is formed by extruding a molten synthetic resin from an extruder. The present invention relates to a method for obtaining thick films.

(従来技術) 一般に、押出機から合成樹脂を押出してフィルムに形成
するものにあっては、引取リローラの回転速度を変化さ
せることによって、フィルム厚ぞを調整しているのであ
るが、従来では、ダイヤルデージでそのフィルム厚を測
定し、その測定値を基準に引取リローラの回転速度を調
整するようにしている。
(Prior Art) In general, when a synthetic resin is extruded from an extruder to form a film, the film thickness is adjusted by changing the rotational speed of the take-up reroller. The film thickness is measured using a dial dage, and the rotational speed of the take-up reroller is adjusted based on the measured value.

また、押出機のスクリュースピードで押出機からの押出
量を算出し、その算出押出量から算出した引取リローラ
の回転速度に調整するようにしたものもある。
In addition, there is also a method in which the amount of extrusion from the extruder is calculated based on the screw speed of the extruder, and the rotational speed of the take-up reroller is adjusted from the calculated amount of extrusion.

(解決しようとする問題点) ダイヤルデージでフィルム厚を測定してローラ速度を調
整するものでは、作業者の熟練度や体調等によって測定
値にバラ付とが生じ、製品としてのフィルム厚さもバラ
付くという問題がある。
(Problem to be solved) When the roller speed is adjusted by measuring the film thickness with a dial gauge, the measured values may vary depending on the skill level and physical condition of the worker, and the film thickness as a product may also vary. There is a problem with sticking.

また、スクリュースピードから時間当りの押出量を算出
し、その算出した押出量を基準にローラ回転速度を設定
するものでは、押出機内での目詰まり等によって算出押
出量と実際の押出量とに差が生じ、製品としてのフィル
ム厚さが変動するという問題がある。
In addition, in the case where the extrusion amount per hour is calculated from the screw speed and the roller rotation speed is set based on the calculated extrusion amount, there may be a difference between the calculated extrusion amount and the actual extrusion amount due to clogging in the extruder. This causes a problem in that the thickness of the film as a product fluctuates.

(問題点を解決するための手段) 本発明は、全長に亘ってフィルムを所望の膜厚lこ形成
するために、押出′a+こ樹脂材料を一定重量づつ間欠
的に自動供給するようにし、押出筒に供給された樹脂材
料を消費する時間、あるいは、一定時間内での供給回数
を測定することにより、押出機からの単位時間当りの押
出量を実測するようにし、この実測値と予め設定されて
いる設定値とを比較して、引取リローラの回転速度を調
整制御するようにしたことを特徴とするものである。
(Means for Solving the Problems) The present invention automatically supplies extruded resin material intermittently in constant weight increments in order to form a film with a desired thickness over the entire length. The amount of extrusion per unit time from the extruder is actually measured by measuring the consumption time of the resin material supplied to the extrusion tube or the number of times it is supplied within a certain period of time, and this actual value is compared with the preset value. This feature is characterized in that the rotational speed of the take-up reroller is adjusted and controlled by comparing it with the set value that has been set.

(作 用) 本発明では、間欠的に供給された一定重量の樹脂材料を
消費する時間を検出すること、あるいは一定時間内に一
定重量の樹脂材料を押出筒に何回供給したかを検出する
ことによって、押出機から実際に押出されている時間当
りの樹脂量を算出し、この算出押出量と予め設定されて
いるフィルム幅、膜厚とから、時間当りの引取り長を算
出して、その引取り長となるように引取りローラの回転
速度を調整制御することになる。この場合、押出量は実
測値となることから、製品の膜厚は所望値に安定する。
(Function) In the present invention, it is possible to detect the time taken to consume a certain weight of resin material that is intermittently supplied, or to detect how many times a certain weight of resin material is fed to the extrusion tube within a certain period of time. By this, the amount of resin actually extruded from the extruder per hour is calculated, and from this calculated extrusion amount and the preset film width and film thickness, the take-off length per hour is calculated. The rotational speed of the take-off roller is adjusted and controlled so that the take-off length is achieved. In this case, since the extrusion amount is the actually measured value, the film thickness of the product is stabilized at the desired value.

(実施例) 第1図は本発明方法のフローチャート、第3図はインフ
レーション方式による合成樹脂シート製造装置の示す概
略構成図である。
(Example) FIG. 1 is a flowchart of the method of the present invention, and FIG. 3 is a schematic diagram showing a synthetic resin sheet manufacturing apparatus using an inflation method.

この樹脂シート製造装置(1)は、内部に螺旋搬送軸(
2)を軸心方向に配置してなる押出筒(3)と、この押
出筒(3)から押出された溶融合成樹脂を引き取る引取
リローラ(4)と、引取リローラ(4)で引取られた合
成樹脂シートを巻取る巻取り部(5)と、押出筒(3)
1こ粒状の合成樹脂材料を供給する原料供給具(6)と
からなっており、押出筒(3)のシリンダ一部分にはヒ
ータ(図示せず)が配置されていて、押出筒(3)内に
供給された合成樹脂材料は、押出筒(3)内を移送され
る間に溶融し、押出筒(3)の先端部に配置したスクリ
ーン(7)を通った後、グイ(8)から筒状に押出され
るようになっている。
This resin sheet manufacturing device (1) has a spiral conveyance shaft (
2) arranged in the axial direction; a take-up reroller (4) that takes over the molten synthetic resin extruded from the extruder reroller (3); A winding section (5) that winds up a resin sheet and an extrusion tube (3)
It consists of a raw material supply tool (6) that supplies granular synthetic resin material, and a heater (not shown) is arranged in a part of the cylinder of the extrusion tube (3), and a heater (not shown) is arranged in a part of the cylinder of the extrusion tube (3). The synthetic resin material supplied to the tube melts while being transferred inside the extrusion tube (3), passes through the screen (7) placed at the tip of the extrusion tube (3), and is then transferred from the guide (8) to the tube. It is extruded in a shape.

原料供給具(6)は、ホッパ=(9)の下端と押出筒(
3)の基端部に形成した材料投入口(10)とを連通接
続する材料供給管(11)の途中に材料定量供給装置(
12)を設けて構成しである。この材料定量供給装置(
12)は、それぞれエアシリンダ(13)(14)で駆
動される上蓋(15)と下蓋(16)とを有しており、
上蓋(15)と下蓋(16)とを択一的に交互に開閉さ
せることにより、上蓋(15)と下蓋(16)及び材料
供給管(11)の内周壁で形成される空間の容積を升と
して、一定容積の合成樹脂材料を材料投入口(10)に
落下供給するよ)にしである。この升部分に升内容積調
節装置(21)が配設してあり、この升内容積調節装置
(21)kこよI)、比重や形状の異なる材料を使用す
る場合に、升内容積を調整して重量を定量化して材料を
材料供給口(10)に供給できるようにしである。
The raw material supply tool (6) is connected to the lower end of the hopper (9) and the extrusion tube (
A material quantitative supply device (
12). This material quantitative supply device (
12) has an upper lid (15) and a lower lid (16) driven by air cylinders (13) and (14), respectively,
By selectively and alternately opening and closing the upper lid (15) and the lower lid (16), the volume of the space formed by the upper lid (15), the lower lid (16), and the inner circumferential wall of the material supply pipe (11) can be increased. A certain volume of synthetic resin material is dropped into the material input port (10) using a volume of . An internal volume adjusting device (21) is installed in this square section, and this internal volume adjusting device (21) adjusts the internal volume when using materials with different specific gravity or shape. This allows the material to be supplied to the material supply port (10) by quantifying its weight.

材料定量供給装置(12)と材料投入口(10)との開
の材料供給路中に上下一対の光電式材料検出具(17)
(18)が上下に適当間隔距でて配置してあり、押出筒
(3)から溶融合成樹脂が押出されることに伴なって材
料供給路中に蓄積されている材料が降下して、材料供給
路中に蓄積されている材料が一定量以下になったことを
下側材料検出共(17)が検出すると、その検出信号に
基づ軽材料定量供給装置(12)の下蓋駆動用エアシリ
ンダ(13)を進出作動させて下蓋(16)を開作動さ
せ、上側材料検出共(18)が落下した材料が材料供給
路中に一定高さに蓄積されたことを検出すると、その検
出信号に基づ外下M、(16)を閉作動させる。下蓋駆
動用エアシリンダ(13)の基端寄り部には近接スイッ
チ(19)が設けてあり、エアシリンダ(13)が退入
移動して下蓋(16)を閉状態にすると、近接スイッチ
(19)が作動して上蓋駆動用エアシリンダ(14)が
進出作動して上II(15)を開状態にし、ホッパー(
9)内の材料を材料定量供給装置(12)に落下させる
。この上蓋(15)はタイマー(20)によって閉作動
するようにしである。
A pair of upper and lower photoelectric material detectors (17) are installed in the open material supply path between the material quantitative supply device (12) and the material input port (10).
(18) are arranged vertically at appropriate intervals, and as the molten synthetic resin is extruded from the extrusion cylinder (3), the material accumulated in the material supply path descends, and the material When the lower material detector (17) detects that the amount of material accumulated in the supply path has become less than a certain amount, the air for driving the lower lid of the light material quantitative supply device (12) is activated based on the detection signal. When the cylinder (13) is advanced and the lower cover (16) is opened, the upper material detector (18) detects that the fallen material has accumulated at a certain height in the material supply path. Based on the signal, the outer lower M (16) is operated to close. A proximity switch (19) is provided near the base end of the lower lid driving air cylinder (13), and when the air cylinder (13) moves in and out to close the lower lid (16), the proximity switch (19) is activated, the upper lid driving air cylinder (14) is advanced and the upper II (15) is opened, and the hopper (
9) Drop the material in the container into the material quantitative supply device (12). This upper lid (15) is closed by a timer (20).

次に、上記装置を使用して、フィルム膜厚を制御する方
法を述べる。
Next, a method for controlling film thickness using the above-mentioned apparatus will be described.

先ず、予備作業として、求めるフィルムの幅(w)と厚
み(1)及び材料の密度(ρ)をマイクロコンピュータ
(M)に入力する。一方、充電式材料検出共(17)(
1B)をマイクロコンピュータ(M)に接続し、光電式
材料検出共(17)の作動間隔から一定容量の樹脂材料
の消費時間(T)を検出手段(D)で検出し、その消費
時間(T)と材料定量供給装置(12)の容積(V)と
から、押出筒(3)での単位時間当りの押出量を演算手
段(O)で算出する。そして、この算出押出量と予め入
力しである所望膜厚(1)と膜幅(111)の積とを比
較手段(C)で比較して演算することにより、算出押出
量に対応する単位時間当り引取り−フ− 量を算出し、この引取り量となるように、引取りローラ
(4)の回転速度を制御する。
First, as a preliminary operation, the width (w) and thickness (1) of the desired film and the density (ρ) of the material are input into the microcomputer (M). On the other hand, rechargeable material detection (17) (
1B) is connected to the microcomputer (M), the consumption time (T) of a certain amount of resin material is detected by the detection means (D) from the operation interval of the photoelectric material detection (17), and the consumption time (T ) and the volume (V) of the material quantitative supply device (12), the amount of extrusion per unit time in the extrusion tube (3) is calculated by the calculation means (O). Then, by comparing and calculating this calculated extrusion amount with the product of the desired film thickness (1) and membrane width (111), which are input in advance, by the comparison means (C), the unit time corresponding to the calculated extrusion amount is calculated. A hit take-off amount is calculated, and the rotational speed of the take-off roller (4) is controlled so as to achieve this take-up amount.

この場合、上側充電式検出共(18)が作動した後、上
側充電式検出共(17)が作動するまでの時間差で消費
時間を検出するようにしてもよい。
In this case, the consumed time may be detected based on the time difference between when the upper rechargeable detector (18) is activated and when the upper rechargeable detector (17) is activated.

また、一定時間内に材料定量供給装置(12)が何回作
動したかを検出し、この検出結果に基づいて単位時間当
りの材料消費量を演算するようにしてもよい。
Alternatively, it may be possible to detect how many times the material quantitative supply device (12) is operated within a certain period of time, and calculate the material consumption amount per unit time based on the detection result.

以上要するに、本発明方法は、インフレーション法やT
ダイ法による押出筒(3)からの押出量に対応して押出
筒(3)に取り込まれる樹脂材料を、材料投入口(10
)に一定容量づつ間欠的に供給し、この一定量の材料が
消費される時間から、押出筒(3)から実際に押出され
ている時間当りの押出量を算出し、この実際に押出され
ている押出量から所望の膜厚及び膜幅に対応する引取り
スピードを算出して、その引取りスピードとなるように
引取リローラの回転数を制御するようにしたものである
In summary, the method of the present invention is based on the inflation method and T
The resin material taken into the extrusion tube (3) in accordance with the amount of extrusion from the extrusion tube (3) by the die method is transferred to the material input port (10).
) is intermittently supplied at a constant volume to The take-off speed corresponding to the desired film thickness and film width is calculated from the extrusion amount, and the rotation speed of the take-off reroller is controlled to achieve the take-off speed.

(効 果) 本発明では、一定量づつ間欠的に供給されている材料の
消費時間から、実際の押出量を算出するようにしている
ので、押出筒内に樹脂材料が膠着していたり、スクリー
ンが目詰まりしたりしていても、グイから押出されてい
る押出量を正確に測定することができる。さらに、実際
の押出量から所望膜厚になる引取り速度を算出して、引
取りローラの回転速度を制御するようにしているので、
押出筒内での押出し速度に変動があっても、製品フィル
ムの膜厚を一定に維持することがで終る。
(Effects) In the present invention, the actual extrusion amount is calculated from the consumption time of the material that is intermittently supplied at a constant rate. Even if the goo is clogged, the amount being extruded from the goo can be accurately measured. Furthermore, since the take-up speed at which the desired film thickness is achieved is calculated from the actual extrusion amount and the rotation speed of the take-up roller is controlled,
Even if the extrusion speed within the extrusion cylinder fluctuates, the thickness of the product film can be maintained constant.

さらに、押出量から引取り速度を算出してローラ回転速
度を制御するものであるから、作業者の熟練度や体調に
影響されることなく、一定膜厚となるように引取りスピ
ードを設定することができる。
Furthermore, since the roller rotation speed is controlled by calculating the take-up speed from the extrusion amount, the take-up speed can be set to maintain a constant film thickness without being affected by the operator's skill level or physical condition. be able to.

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

第1図は制御手順を示すフローチャート、第2図はイン
フレーション方式によるフィルム製造装置の概略構成図
である。 3・・・押出筒、4・・・引取りローラ、D・・・消費
時間検出手段、0・・・押出量演算手段、C・・・比較
手段。
FIG. 1 is a flowchart showing a control procedure, and FIG. 2 is a schematic diagram of a film manufacturing apparatus using an inflation method. 3... Extrusion tube, 4... Take-up roller, D... Consumption time detection means, 0... Extrusion amount calculation means, C... Comparison means.

Claims (1)

【特許請求の範囲】[Claims] 1、押出筒(3)から合成樹脂を押出して合成樹脂フィ
ルムに形成するにあたり、押出筒(3)に一定重量の樹
脂材料を間欠的に自動供給し、この押出筒(3)に供給
された一定重量の樹脂材料を消費する時間と単位時間当
りに押出筒(3)に樹脂材料を供給する供給回数とのい
ずれか一方を検出手段(D)で検出し、検出手段(D)
からの出力信号で押出筒(3)からの単位時間当りの押
出量を演算手段(O)で計算し、演算手段(O)からの
出力と予め与えられている設定値とを比較手段(C)で
比較し、比較手段(C)からの出力に基づいて、引取り
ローラ(4)の回転速度を制御することによりフィルム
シートの肉厚を一定厚さに形成するようにしたことを特
徴とする合成樹脂フィルム製造装置におけるフィルム厚
さ制御方法
1. When extruding synthetic resin from the extrusion tube (3) to form a synthetic resin film, a constant weight of resin material is automatically and intermittently supplied to the extrusion tube (3), and the resin material is intermittently supplied to the extrusion tube (3). The detection means (D) detects either the time for consuming a certain weight of the resin material or the number of times the resin material is supplied to the extrusion cylinder (3) per unit time, and the detection means (D)
The calculation means (O) calculates the amount of extrusion per unit time from the extrusion tube (3) using the output signal from the extrusion tube (3), and compares the output from the calculation means (O) with a preset value. ), and the thickness of the film sheet is formed to a constant thickness by controlling the rotational speed of the take-up roller (4) based on the output from the comparison means (C). Film thickness control method in synthetic resin film manufacturing equipment
JP61090760A 1986-04-18 1986-04-18 Controlling film thickness in apparatus for manufacturing synthetic resin film Pending JPS62246713A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61090760A JPS62246713A (en) 1986-04-18 1986-04-18 Controlling film thickness in apparatus for manufacturing synthetic resin film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61090760A JPS62246713A (en) 1986-04-18 1986-04-18 Controlling film thickness in apparatus for manufacturing synthetic resin film

Publications (1)

Publication Number Publication Date
JPS62246713A true JPS62246713A (en) 1987-10-27

Family

ID=14007560

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61090760A Pending JPS62246713A (en) 1986-04-18 1986-04-18 Controlling film thickness in apparatus for manufacturing synthetic resin film

Country Status (1)

Country Link
JP (1) JPS62246713A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6424721A (en) * 1987-07-21 1989-01-26 Shikoku Maruyasu Kk Extrusion molding apparatus capable of automatically taking up
JPS6426424A (en) * 1987-07-22 1989-01-27 Shikoku Maruyasu Kk Extrusion molding method capable of performing automatic take-out control
JPH01168423A (en) * 1987-12-25 1989-07-03 Fukusuke Kogyo Kk Control device for film thickness
JPH03227217A (en) * 1990-01-31 1991-10-08 Sekisui Chem Co Ltd Thickness controlling device in multilayer inflation molding line
JPH03261538A (en) * 1990-03-09 1991-11-21 Toyo Denki Kk Draw-off controlling apparatus for inflation film manufacturing machine

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60218713A (en) * 1984-04-13 1985-11-01 昭和電線電纜株式会社 Thickness regulator for cable

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60218713A (en) * 1984-04-13 1985-11-01 昭和電線電纜株式会社 Thickness regulator for cable

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6424721A (en) * 1987-07-21 1989-01-26 Shikoku Maruyasu Kk Extrusion molding apparatus capable of automatically taking up
JPS6426424A (en) * 1987-07-22 1989-01-27 Shikoku Maruyasu Kk Extrusion molding method capable of performing automatic take-out control
JPH01168423A (en) * 1987-12-25 1989-07-03 Fukusuke Kogyo Kk Control device for film thickness
JPH03227217A (en) * 1990-01-31 1991-10-08 Sekisui Chem Co Ltd Thickness controlling device in multilayer inflation molding line
JPH03261538A (en) * 1990-03-09 1991-11-21 Toyo Denki Kk Draw-off controlling apparatus for inflation film manufacturing machine

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