JPH091638A - Method and apparatus for controlling to extrude in extruder - Google Patents
Method and apparatus for controlling to extrude in extruderInfo
- Publication number
- JPH091638A JPH091638A JP7159568A JP15956895A JPH091638A JP H091638 A JPH091638 A JP H091638A JP 7159568 A JP7159568 A JP 7159568A JP 15956895 A JP15956895 A JP 15956895A JP H091638 A JPH091638 A JP H091638A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- extruder
- extrusion
- rubber
- arithmetic unit
- 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
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
- B29C48/25—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
- B29C2948/92209—Temperature
-
- 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
- B29C2948/92361—Extrusion unit
- B29C2948/9238—Feeding, melting, plasticising or pumping zones, e.g. the melt itself
- B29C2948/924—Barrel or housing
-
- 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
- B29C2948/92361—Extrusion unit
- B29C2948/92409—Die; Nozzle zone
-
- 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
- B29C2948/9258—Velocity
-
- 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
- B29C2948/9258—Velocity
- B29C2948/9259—Angular velocity
-
- 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
- B29C2948/92704—Temperature
-
- 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
- B29C2948/92876—Feeding, melting, plasticising or pumping zones, e.g. the melt itself
- B29C2948/92885—Screw or gear
-
- 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
- B29C2948/92876—Feeding, melting, plasticising or pumping zones, e.g. the melt itself
- B29C2948/92895—Barrel or housing
-
- 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
-
- 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
- B29C2948/92933—Conveying, transporting or storage of articles
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、ゴム材料や合成樹脂
材料等を押出す押出し機における押出し制御方法及びそ
の装置に係わり、更に詳しくは次の押出し材料の押出し
初期における重量不足や、形状変化を有効に防止させた
押出し機における押出し制御方法及びその装置に関する
ものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an extrusion control method and apparatus in an extruder for extruding rubber materials, synthetic resin materials and the like, and more specifically, to a shortage of weight and shape change of the next extrusion material at the initial stage of extrusion. The present invention relates to an extrusion control method and apparatus for an extruder that effectively prevents the above.
【0002】[0002]
【従来の技術】従来、ゴム材料や合成樹脂材料等のゴム
状弾性材料を押出し成形する場合、1ロット当たりの押
出し成形が終了すると、押出し機のヘッド内にゴム状弾
性材料を残したまま、一旦押出し機を停止する。そし
て、次のサイズを押し出すために、押出し機を再起動さ
せると、押出し初期はヘッド内に残留していたゴム状弾
性材料の影響によって押出し形状不良や、単位重量不良
が起きて、リターンが多量に発生すると言う問題があっ
た。2. Description of the Related Art Conventionally, when a rubber-like elastic material such as a rubber material or a synthetic resin material is extrusion-molded, when the extrusion molding per lot is completed, the rubber-like elastic material remains in the head of the extruder. Stop the extruder once. Then, when the extruder is restarted to push out the next size, the extrusion shape defect or unit weight defect occurs due to the influence of the rubber-like elastic material remaining in the head in the initial stage of extrusion, resulting in a large amount of returns. There was a problem that it occurs in.
【0003】[0003]
【発明が解決しようとする問題点】そこで、押出初期の
押出し形状不良や、単位重量不良を防止させるために、
例えば、特開平4ー16324号公報に開示されている
ように、押出し機の停止時間をパラメータとして押出し
機のスクリュー回転数及びストレッチコンベヤーの速度
をコントロールする方法が提案されている。Therefore, in order to prevent defective extrusion shape in the initial stage of extrusion and defective unit weight,
For example, as disclosed in Japanese Patent Application Laid-Open No. 4-16324, a method has been proposed in which the screw rotation speed of the extruder and the speed of the stretch conveyor are controlled with the stop time of the extruder as a parameter.
【0004】然しながら、このような従来の方法は、押
出し開始前の停止時間のみに着目し、押出しの重量バラ
ツキがゴム材料の種類や投入温度及び安定状態までの平
衡温度等の温度により発生していることに着目していな
い。そのため、季節変動やゴム材料のロット間バラツキ
等の要因により、安定状態が微妙に異なるために発生す
るゴム重量バラツキに対応出来ないと言う問題があっ
た。However, in such a conventional method, paying attention only to the stop time before the start of extrusion, the variation in the weight of the extrusion occurs due to the kind of the rubber material, the feeding temperature and the temperature such as the equilibrium temperature until the stable state. I'm not paying attention to being there. Therefore, there is a problem that it is not possible to cope with the variation in rubber weight caused by a slight difference in the stable state due to factors such as seasonal variation and variation in lots of rubber materials.
【0005】この発明は、かかる従来の課題に着目して
案出されたもので、押出し機温調温度や押出し機周辺の
雰囲気温度や、投入ゴム温度または過去のデータから、
押出し機の稼働停止中に、次に押出されるサイズの押出
し安定時のゴム温度を演算装置に引出し、この演算装置
に入力されたデータと、押出し機のスタート直前のヘッ
ド内ゴム温度を比較演算し、スクリュー回転数や引取り
コンベヤの送り速度を制御することにより、押出し初期
の押出し形状不良や、単位重量不良を有効に防止し、更
にリターンを減少させることが出来る押出し機における
押出し制御方法及びその装置を提供することを目的とす
るものである。The present invention has been devised in view of the above-mentioned conventional problems. From the extruder temperature control temperature, the ambient temperature around the extruder, the input rubber temperature or past data,
While the extruder is not operating, the rubber temperature at the next extrusion size when the extrusion is stable is drawn out to the arithmetic unit, and the data input to this arithmetic unit is compared with the rubber temperature in the head just before the extruder starts. However, by controlling the screw rotation speed and the feeding speed of the take-up conveyor, it is possible to effectively prevent the extrusion shape defect in the initial stage of extrusion and the unit weight defect, and to further reduce the return, and the extrusion control method in the extruder. The purpose is to provide the device.
【0006】また、この発明の他の目的は、予め、ゴム
の種類毎に押出し中のゴムの安定温度と単位時間当たり
のゴム温度上昇率とをデータベースに蓄積しておき、ま
た押出し直前の押出し機ヘッド内のゴム温度を測定し、
この押出し機ヘッド内のゴム温度と前記安定温度とを比
較演算することにより、平衡温度に達するまでの温度差
及び時間を求め、この時間に基づき、押出し機のスクリ
ュー回転数を制御することにより、ゴムの種類が異なっ
ても、過剰な回転数制御や、不足の回転数制御がなくな
り、常に安定した押出し制御を行うことが出来る押出し
機における押出し制御方法及びその装置を提供すること
を目的とするものである。Another object of the present invention is to store in advance a stable temperature of the rubber being extruded and a rubber temperature rise rate per unit time for each type of rubber in a database, and to extrude just before the extrusion. Measure the rubber temperature in the machine head,
By comparing and calculating the rubber temperature in the extruder head and the stable temperature, the temperature difference and time until reaching the equilibrium temperature is obtained, and based on this time, by controlling the screw rotation speed of the extruder, It is an object of the present invention to provide an extrusion control method and apparatus for an extruder, which can eliminate excessive rotation speed control and insufficient rotation speed control even when the type of rubber is different, and can always perform stable extrusion control. It is a thing.
【0007】[0007]
【課題を解決するための手段】この発明は上記目的を達
成するため、押出し機温調温度を測定する測定手段と、
押出しヘッド内のゴム温度を測定する測定手段と、投入
ゴム温度を測定する測定手段とを備えた押出し機と、押
出し機周辺の雰囲気温度を測定する測定手段と、過去の
押出し安定状態における押出しヘッド内のゴム温度と、
このゴム温度に対する押出し機のスクリュー回転数及び
引取りコンベヤの速度を予め設定並びに蓄積するデータ
ベースと、押出し機温調温度,押出しヘッド内のゴム温
度,押出し機周辺の雰囲気温度と、過去の押出し安定状
態における押出しヘッド内のゴム温度とを比較演算する
演算装置とからなり、前記演算装置と、押出し機のスク
リュー回転駆動モータ及び引取りコンベヤの駆動モータ
とを接続したことを要旨とするものである。In order to achieve the above object, the present invention provides a measuring means for measuring an extruder temperature control temperature,
An extruder equipped with a measuring means for measuring the rubber temperature in the extrusion head, a measuring means for measuring the input rubber temperature, a measuring means for measuring the ambient temperature around the extruder, and an extrusion head in a past stable extrusion state. The rubber temperature inside,
A database that presets and accumulates the screw rotation speed of the extruder and the speed of the take-up conveyor with respect to this rubber temperature, the temperature control temperature of the extruder, the rubber temperature inside the extruder head, the ambient temperature around the extruder, and the past extrusion stability. It is composed of an arithmetic device for performing a comparative arithmetic operation with the rubber temperature in the extrusion head in a state, and the gist is that the arithmetic device is connected to the screw rotation drive motor of the extruder and the drive motor of the take-up conveyor. .
【0008】[0008]
【発明の作用】この発明は上記のように構成され、押出
し機の制御装置のデータベースに、過去の押出し安定状
態における押出しヘッド内のゴム温度と、このゴム温度
に対する押出し機のスクリュー回転数及び引取りコンベ
ヤの速度を予め設定し、次の押出しまでの押出し機の稼
働停止時に、次の押出しサイズに対応したゴム安定押出
し温度をデータベースから引き出して演算装置に入力す
ると共に、押出し機温調温度と押出し機周辺の雰囲気温
度,投入ゴム温度を測定して演算装置に入力し、更に次
の押出し機のスタート直前における押出しヘッド内のゴ
ム温度を演算装置に入力して比較演算し、この演算装置
で比較演算した温度差に基づき、演算装置からの指令に
より、前記押出し機のスクリュー回転数及び引取りコン
ベヤの速度を制御することにより、押出し初期の押出し
形状不良や、単位重量不良を有効に防止し、更にリター
ンを減少させることが出来るものである。The present invention is configured as described above, and the rubber temperature in the extrusion head in the past stable extrusion state and the screw rotation speed and the pulling speed of the extruder with respect to this rubber temperature are stored in the database of the extruder control device. The speed of the take-up conveyor is set in advance, and when the operation of the extruder until the next extrusion is stopped, the rubber stable extrusion temperature corresponding to the next extrusion size is retrieved from the database and input to the arithmetic unit, and the extruder temperature control temperature and The ambient temperature around the extruder and the temperature of the input rubber are measured and input to the arithmetic unit, and the rubber temperature inside the extrusion head immediately before the start of the next extruder is input to the arithmetic unit for comparison calculation. Based on the calculated temperature difference, the screw speed of the extruder and the speed of the take-up conveyor are controlled by the command from the arithmetic unit. Rukoto, the extrusion shape defects and extrusion early, preventing unit weight defects effectively, those which can further reduce the return.
【0009】また、ゴムの種類毎に過去の押出し中のゴ
ムの安定状態における温度と、単位時間当たりのゴム温
度上昇率とを、予め押出し機の制御装置のデータベース
に入力しておき、次に押出すゴムの種類に対応したゴム
の安定状態における温度と、単位時間当たりのゴム温度
上昇率とを引出して演算装置に入力すると共に、次の押
出し直前の押出し機ヘッド内のゴム温度を測定して、そ
の温度を演算装置に入力し、該演算装置で、前記ゴムの
安定状態における温度と押出し直前の押出し機ヘッド内
のゴム温度との温度差と、単位時間当たりのゴム温度上
昇率とから一定温度に達するまでの時間を演算により求
め、この時間に基づき、押出し機のスクリュー回転数を
制御することにより、ゴムの種類が異なっても、過剰な
回転数制御や、不足の回転数制御がなくなり、常に安定
した押出し制御を行うことが出来るものである。Further, the temperature in the past stable state of rubber during extrusion and the rate of rise in rubber temperature per unit time are inputted in advance into the database of the control device of the extruder for each type of rubber, and then The temperature in the stable state of the rubber corresponding to the type of rubber to be extruded and the rubber temperature rise rate per unit time are extracted and input to the arithmetic unit, and the rubber temperature in the extruder head immediately before the next extrusion is measured. Then, the temperature is input to an arithmetic unit, and the arithmetic unit calculates the temperature difference between the temperature in the stable state of the rubber and the rubber temperature in the extruder head immediately before extrusion, and the rubber temperature increase rate per unit time. The time required to reach a certain temperature is calculated, and the screw speed of the extruder is controlled based on this time. There is no rotational speed control of, is always capable of performing stable extrusion control.
【0010】[0010]
【発明の実施例】以下、添付図面に基づき、この発明の
実施例を説明する。図1は、この発明にかかる押出し制
御方法を実施するための押出し機における押出し制御装
置の概略構成図を示し、前記3台の押出し機1a,1
b,1cの内部には、押出し機温調温度を測定する測定
手段2a,2b,2cが取付けられ、また押出しヘッド
3内には、押出しヘッド3内のゴム温度を測定する測定
手段4が取付けられている。Embodiments of the present invention will be described below with reference to the accompanying drawings. FIG. 1 is a schematic configuration diagram of an extrusion control device in an extruder for carrying out the extrusion control method according to the present invention, in which the three extruders 1a, 1
Measuring means 2a, 2b, 2c for measuring the temperature controlled by the extruder are attached inside b, 1c, and measuring means 4 for measuring the rubber temperature inside the extrusion head 3 is attached inside the extrusion head 3. Has been.
【0011】前記3台の押出し機1a,1b,1cに
は、それぞれ押出しスクリューを回転駆動させる駆動モ
ータM1 ,M2 ,M3 が接続され、押出しヘッド3の前
方には駆動モータMにより回転駆動する引取りコンベヤ
5が水平に設置されている。前記押出しヘッド3の外部
には、押出し機周辺の雰囲気温度を測定する測定手段6
が設置されると共に、過去の押出し安定状態における押
出しヘッド内のゴム温度と、このゴム温度に対する押出
し機1a,1b,1cのスクリュー回転数及び引取りコ
ンベヤ5の速度を予め設定並びに蓄積するデータベース
7と、押出し機温調温度,押出しヘッド内のゴム温度,
押出し機周辺の雰囲気温度と、過去の押出し安定状態に
おける押出しヘッド内のゴム温度とを比較演算する演算
装置8とからなる押出し制御装置が設置されている。Drive motors M 1 , M 2 and M 3 for rotating and driving the extrusion screws are connected to the three extruders 1a, 1b and 1c, respectively. The drive motor M rotates in front of the extrusion head 3. The driven take-up conveyor 5 is installed horizontally. Outside the extrusion head 3, a measuring means 6 for measuring the ambient temperature around the extruder.
Is installed, and a database 7 for presetting and accumulating the rubber temperature in the extrusion head in the past stable extrusion state, the screw rotation speed of the extruders 1a, 1b, 1c and the speed of the take-up conveyor 5 with respect to this rubber temperature. And extruder temperature control, rubber temperature in the extrusion head,
An extrusion controller including an arithmetic unit 8 for comparing and calculating the ambient temperature around the extruder and the rubber temperature in the extrusion head in the past stable extrusion state is installed.
【0012】前記演算装置8は、押出し機1a,1b,
1cの回転駆動モータM1 ,M2 ,M3 及び引取りコン
ベヤ5の駆動モータMとを接続され、演算装置8からの
指令により、前記押出し機1a,1b,1cのスクリュ
ー回転数及び引取りコンベヤ5の速度を制御するように
構成されている。この発明は、上記のように構成され、
押出しヘッド3内のゴム温度による押出し初期安定制御
を行う場合には、次のような方法により行うものであ
る。The arithmetic unit 8 includes extruders 1a, 1b,
The rotation drive motors M 1 , M 2 and M 3 of 1c and the drive motor M of the take-up conveyor 5 are connected, and the screw rotation speed and take-up of the extruders 1a, 1b, 1c are instructed by the arithmetic unit 8. It is arranged to control the speed of the conveyor 5. The present invention is configured as described above,
When performing initial stability control of extrusion by the temperature of rubber in the extrusion head 3, the following method is used.
【0013】即ち、押出し機1a,1b,1cの制御装
置のデータベース7に、過去の押出し安定状態における
押出しヘッド3内のゴム温度と、このゴム温度に対する
押出し機1a,1b,1cのスクリュー回転数及び引取
りコンベヤ5の速度を予め設定並びに蓄積させておく。
次の押出しまでの押出し機1a,1b,1cの稼働停止
時に、次の押出しサイズに対応したゴム安定押出し温度
をデータベース7から引き出して演算装置8に入力する
と共に、押出し機温調温度と押出し機周辺の雰囲気温度
と投入ゴム温度とを測定して演算装置8に入力し、更に
次の押出し機のスタート直前における押出しヘッド内の
ゴム温度を演算装置に入力して比較演算する。That is, in the database 7 of the control device of the extruders 1a, 1b, 1c, the rubber temperature in the extrusion head 3 in the past stable extrusion state and the screw rotation speed of the extruders 1a, 1b, 1c with respect to this rubber temperature are stored. And the speed of the take-up conveyor 5 is set and accumulated in advance.
When the operation of the extruders 1a, 1b, 1c until the next extrusion is stopped, the rubber stable extrusion temperature corresponding to the next extrusion size is retrieved from the database 7 and input to the arithmetic unit 8, and the extruder temperature control temperature and the extruder The ambient atmospheric temperature and the input rubber temperature are measured and input to the arithmetic unit 8, and the rubber temperature in the extrusion head immediately before the start of the next extruder is input to the arithmetic unit for comparison calculation.
【0014】そして、この演算装置8で比較演算した温
度差に基づき、演算装置8からの指令により、前記押出
し機1a,1b,1cのスクリュー回転数及び引取りコ
ンベヤの速度を制御することにより、押出し初期の押出
し形状不良や、単位重量不良を有効に防止し、更にリタ
ーンを減少させることが出来るものである。この押出し
制御方法を、図2及び図3に示すタイミングチャートを
参照しながら更に具体的に説明すると、横軸が時間の流
れ方向を示し、Aサイズの材料の押出し作業が終了する
と、押出し機を一旦停止させて、その停止時間中に、次
のサイズBの押出し材料に対応した押出しヘッドに交換
する。Based on the temperature difference compared and calculated by the arithmetic unit 8, the screw speeds of the extruders 1a, 1b and 1c and the speed of the take-up conveyor are controlled by a command from the arithmetic unit 8. It is possible to effectively prevent a defective extrusion shape in the initial stage of extrusion and a defective unit weight, and further reduce the return. This extrusion control method will be described more specifically with reference to the timing charts shown in FIGS. 2 and 3. When the horizontal axis indicates the flow direction of time and the extrusion work of the A size material is completed, the extruder is operated. It is stopped once, and during the stop time, it is replaced with an extrusion head corresponding to the next size B extrusion material.
【0015】この押出し機の停止時間中に、押出しダイ
ス内に残留していた押出し材料の温度は、押出しヘッド
の温度低下と共に押出し安定状態における温度Tよりも
ΔTだけ低下してT1 となり、また押出し材料の重量
も、目標重量よりもAだけ軽くなる。このように押出し
機の停止時間中に、押出しヘッドの温度が安定状態にお
ける温度Tよりも低下した場合、押出し機1a,1b,
1cの内部に設けた測定手段2a,2b,2cで測定し
た押出し機温調温度と、押出し機周辺の雰囲気温度と投
入ゴム温度とを測定する測定手段6から雰囲気温度とを
演算装置8に出力し、また過去のデータを予め入力して
あるデータベース7から選択された次のサイズBの押出
し材料に対応したデータを演算装置8に出力する。During the stop time of the extruder, the temperature of the extruded material remaining in the extrusion die is reduced by ΔT from the temperature T in the stable extrusion state to T 1 as the temperature of the extrusion head decreases, and The weight of the extruded material is also A less than the target weight. In this way, when the temperature of the extrusion head is lower than the temperature T in the stable state during the stop time of the extruder, the extruders 1a, 1b,
The extruder temperature control temperature measured by the measuring means 2a, 2b, 2c provided inside 1c, and the atmospheric temperature from the measuring means 6 for measuring the ambient temperature around the extruder and the input rubber temperature are output to the arithmetic unit 8. In addition, data corresponding to the next size B extruded material selected from the database 7 in which the past data is input in advance is output to the arithmetic unit 8.
【0016】そして、次のサイズBの押出し材料を押出
す直前における押出しヘッド3内のゴム温度を測定手段
4を測定して演算装置8に出力する。そして、この発明
では、データベース7から選択されたデータと入力され
た各温度とを比較演算し、比較演算した温度差に基づ
き、演算装置8からの指令により、前記押出し機1a,
1b,1cのスクリュー回転数及び引取りコンベヤの速
度を制御することにより、押出し初期における押出し形
状や、単位重量不良を短期間に終了させ、次のサイズB
の押出し材料における安定押出し状態、即ち、押出しゴ
ムの温度や重量を安定状態に制御するものである。Then, the rubber temperature in the extrusion head 3 immediately before the extrusion material of the next size B is extruded is measured by the measuring means 4 and output to the arithmetic unit 8. Then, in the present invention, the data selected from the database 7 and the respective input temperatures are compared and calculated, and the extruder 1a,
By controlling the screw rotation speed of 1b and 1c and the speed of the take-up conveyor, the extrusion shape in the initial stage of extrusion and the unit weight defect are completed in a short time, and the next size B
The stable extruded state of the extruded material, that is, the temperature and weight of the extruded rubber are controlled to be stable.
【0017】これにより、押出し材料のリターンを減少
させることが出来るものである。即ち、図3に示すよう
に、押出しヘッド3から押出された押出し材料を引取り
コンベヤ5で引取り、ランニングスケール9及び搬送コ
ンベヤ10を通して選別重量計11の位置まで搬送した
後、押出し材料の重量を計量するものである。次に、図
4及び図5は、押出し制御方法の他の実施例を示し、こ
の実施例は、図4に示すように、押出すゴムの種類X,
Y,Zが異なるような場合に、ゴムの種類毎に押出し時
の安定温度(平衡温度)と、単位時間当たりの温度上昇
率が異なることに着目し、押出すゴムの種類X,Y,Z
毎に、そのゴムの種類に対応した制御を行うようにした
ものである。As a result, the return of the extruded material can be reduced. That is, as shown in FIG. 3, the extruded material extruded from the extruding head 3 is taken by the take-up conveyor 5, conveyed through the running scale 9 and the conveyer conveyor 10 to the position of the weighing scale 11, and then the weight of the extruded material is taken. Is to measure. Next, FIGS. 4 and 5 show another embodiment of the extrusion control method. In this embodiment, as shown in FIG.
When Y and Z are different, paying attention to the fact that the stable temperature (equilibrium temperature) at the time of extrusion and the temperature rise rate per unit time are different for each type of rubber, and the type of rubber to be extruded X, Y, Z
Each time, the control corresponding to the type of rubber is performed.
【0018】即ち、ゴムの種類毎に過去の押出し中のゴ
ムの安定状態における温度Tと、単位時間当たりのゴム
温度上昇率とを、予め押出し機の制御装置のデータベー
ス7に入力しておく。そして、次に押出すゴムの種類に
対応したゴムの安定状態における温度Tと、単位時間当
たりのゴム温度上昇率とを引出して演算装置8に入力す
ると共に、次の押出し直前の押出し機ヘッド3内のゴム
温度T1 を測定して、その温度T1 を演算装置8に入力
する。That is, the temperature T of the rubber in a stable state during extrusion in the past and the rubber temperature increase rate per unit time are input in advance to the database 7 of the controller of the extruder for each type of rubber. Then, the temperature T in the stable state of the rubber corresponding to the type of rubber to be extruded next and the rubber temperature increase rate per unit time are extracted and input to the arithmetic unit 8, and the extruder head 3 immediately before the next extrusion is also extracted. The rubber temperature T 1 therein is measured, and the temperature T 1 is input to the arithmetic unit 8.
【0019】前記演算装置8では、前記ゴムの安定状態
における温度Tと押出し直前の押出し機ヘッド内のゴム
温度T1 との温度差ΔTと、単位時間当たりのゴム温度
上昇率とから一定温度に達するまでの時間を演算により
求め、この時間に基づき、押出し機のスクリュー回転数
を制御する。このような制御を行うことによって、ゴム
の種類が異なっても、過剰な回転数制御や、不足の回転
数制御がなくなり、常に安定した押出し制御を行うこと
が出来るものである。In the arithmetic unit 8, the temperature difference ΔT between the temperature T of the rubber in a stable state and the rubber temperature T 1 in the extruder head immediately before extrusion, and the rate of increase in rubber temperature per unit time are used to obtain a constant temperature. The time required to reach it is calculated and the screw speed of the extruder is controlled based on this time. By performing such control, even if the type of rubber is different, excessive rotation speed control and insufficient rotation speed control are eliminated, and stable extrusion control can always be performed.
【0020】[0020]
【発明の効果】この発明は、上記のように押出し機の制
御装置のデータベースに、過去の押出し安定状態におけ
る押出しヘッド内のゴム温度と、このゴム温度に対する
押出し機のスクリュー回転数及び引取りコンベヤの速度
を予め設定し、次の押出しまでの押出し機の稼働停止時
に、次の押出しサイズに対応したゴム安定押出し温度を
データベースから引き出して演算装置に入力すると共
に、押出し機温調温度と押出し機周辺の雰囲気温度を測
定して演算装置に入力し、更に次の押出し機のスタート
直前における押出しヘッド内のゴム温度を演算装置に入
力して比較演算し、この演算装置で比較演算した温度差
に基づき、演算装置からの指令により、前記押出し機の
スクリュー回転数及び引取りコンベヤの速度を制御する
ようにしたので、押出し初期の押出し形状不良や、単位
重量不良を有効に防止でき、更にリターンを減少させる
ことが出来る効果がある。As described above, according to the present invention, in the database of the extruder control device, the rubber temperature in the extrusion head in the past stable extrusion state, the screw rotation speed of the extruder and the take-up conveyor with respect to this rubber temperature. The speed of is set in advance, and when the operation of the extruder until the next extrusion is stopped, the rubber stable extrusion temperature corresponding to the next extrusion size is drawn from the database and input to the arithmetic unit, and the extruder temperature control temperature and extruder The ambient temperature is measured and input to the arithmetic unit, and the rubber temperature in the extrusion head immediately before the start of the next extruder is input to the arithmetic unit for comparison calculation. Based on the instruction from the arithmetic unit, the screw speed of the extruder and the speed of the take-up conveyor are controlled. Early or extrusion shape defects, and unit weight failure it can effectively prevent the effect that can further reduce the return.
【0021】また、予め、ゴムの種類毎に押出し中のゴ
ムの安定温度と単位時間当たりのゴム温度上昇率とをデ
ータベースに蓄積しておき、また押出し直前の押出し機
ヘッド内のゴム温度を測定し、この押出し機ヘッド内の
ゴム温度と前記安定温度とを比較演算することにより、
平衡温度に達するまでの温度差及び時間を求め、この時
間に基づき、押出し機のスクリュー回転数を制御するこ
とにより、ゴムの種類が異なっても、過剰な回転数制御
や、不足の回転数制御がなくなり、常に安定した押出し
制御を行うことが出来る効果がある。Further, the stable temperature of the rubber being extruded and the rate of rise of the rubber temperature per unit time are accumulated in a database in advance for each type of rubber, and the rubber temperature in the extruder head immediately before extrusion is measured. Then, by comparing and calculating the rubber temperature in the extruder head and the stable temperature,
Obtain the temperature difference and time to reach the equilibrium temperature, and control the screw speed of the extruder based on this time to control excessive rotation speed and insufficient rotation speed even if the rubber type is different. Is eliminated, and there is an effect that stable extrusion control can be always performed.
【図1】この発明にかかる押出し制御方法を実施するた
めの押出し機における押出し制御装置の概略構成図であ
る。FIG. 1 is a schematic configuration diagram of an extrusion control device in an extruder for carrying out an extrusion control method according to the present invention.
【図2】この発明にかかる押出し制御方法のタイミング
チャートである。FIG. 2 is a timing chart of the extrusion control method according to the present invention.
【図3】この発明にかかる押出し制御方法のタイミング
チャートである。FIG. 3 is a timing chart of an extrusion control method according to the present invention.
【図4】押出すゴムの種類に対する温度と時間との関係
を示すグラフ説明図である。FIG. 4 is a graph explanatory view showing the relationship between temperature and time with respect to the type of rubber to be extruded.
【図5】この発明の他の押出し制御方法の実施例を示す
タイミングチャートである。FIG. 5 is a timing chart showing an embodiment of another extrusion control method of the present invention.
1a,1b,1c 押出し機 2a,2b,2c 測定手段 3 押出し
ヘッド 4 測定手段 5 引取り
コンベヤ 6 測定手段 7 データ
ベース 8 演算装置 M 駆動モ
ータ M1 ,M2 ,M3 回転駆動モータ1a, 1b, 1c Extruder 2a, 2b, 2c Measuring means 3 Extrusion head 4 Measuring means 5 Take-off conveyor 6 Measuring means 7 Database 8 Computing device M Drive motor M 1 , M 2 , M 3 Rotation drive motor
Claims (3)
過去の押出し安定状態における押出しヘッド内のゴム温
度と、このゴム温度に対する押出し機のスクリュー回転
数及び引取りコンベヤの速度を予め設定し、次の押出し
までの押出し機の稼働停止時に、次の押出しサイズに対
応したゴム安定押出し温度をデータベースから引き出し
て演算装置に入力すると共に、押出し機温調温度と押出
し機周辺の雰囲気温度,投入ゴム温度を測定して演算装
置に入力し、更に次の押出し機のスタート直前における
押出しヘッド内のゴム温度を演算装置に入力して比較演
算し、この演算装置で比較演算した温度差に基づき、演
算装置からの指令により、前記押出し機のスクリュー回
転数及び引取りコンベヤの速度を制御することを特徴と
する押出し機における押出し制御方法。1. A database of a control device of an extruder,
The temperature of the rubber in the extrusion head in the past stable state of extrusion, the screw rotation speed of the extruder and the speed of the take-up conveyor with respect to this rubber temperature are set in advance, and when the operation of the extruder until the next extrusion is stopped, the next extrusion is performed. The rubber stable extrusion temperature corresponding to the size is extracted from the database and input to the arithmetic unit, and the extruder temperature control temperature, the ambient temperature around the extruder and the input rubber temperature are measured and input to the arithmetic unit, and the next extrusion is performed. The rubber temperature in the extrusion head immediately before the start of the machine is input to the arithmetic unit for comparison calculation, and based on the temperature difference compared and calculated by this arithmetic unit, the screw rotation speed and the pulling speed of the extruder are set by the instruction from the arithmetic unit. An extrusion control method in an extruder, characterized by controlling the speed of a take-up conveyor.
安定状態における温度と、単位時間当たりのゴム温度上
昇率とを、予め押出し機の制御装置のデータベースに入
力しておき、次に押出すゴムの種類に対応したゴムの安
定状態における温度と、単位時間当たりのゴム温度上昇
率とを引出して演算装置に入力すると共に、次の押出し
直前の押出し機ヘッド内のゴム温度を測定して、その温
度を演算装置に入力し、該演算装置で、前記ゴムの安定
状態における温度と押出し直前の押出し機ヘッド内のゴ
ム温度との温度差と、単位時間当たりのゴム温度上昇率
とから一定温度に達するまでの時間を演算により求め、
この時間に基づき、押出し機のスクリュー回転数を制御
することを特徴とする押出し機における押出し制御方
法。2. The temperature in a stable state of rubber during extrusion in the past for each type of rubber and the rubber temperature rise rate per unit time are input in advance in the database of the controller of the extruder, and then, The temperature in the stable state of the rubber corresponding to the type of rubber to be extruded and the rubber temperature rise rate per unit time are extracted and input to the arithmetic unit, and the rubber temperature in the extruder head immediately before the next extrusion is measured. Then, the temperature is input to an arithmetic unit, and the arithmetic unit calculates the temperature difference between the temperature in the stable state of the rubber and the rubber temperature in the extruder head immediately before extrusion, and the rubber temperature increase rate per unit time. Calculate the time to reach a certain temperature,
An extrusion control method for an extruder, comprising controlling the screw rotation speed of the extruder based on this time.
と、押出しヘッド内のゴム温度を測定する測定手段とを
備えた押出し機と、押出し機周辺の雰囲気温度を測定す
る測定手段と、投入ゴム温度を測定する測定手段,過去
の押出し安定状態における押出しヘッド内のゴム温度
と、このゴム温度に対する押出し機のスクリュー回転数
及び引取りコンベヤの速度を予め設定並びに蓄積するデ
ータベースと、押出し機温調温度,押出しヘッド内のゴ
ム温度,押出し機周辺の雰囲気温度と、過去の押出し安
定状態における押出しヘッド内のゴム温度とを比較演算
する演算装置とからなり、前記演算装置と、押出し機の
スクリュー回転駆動モータ及び引取りコンベヤの駆動モ
ータとを接続したことを特徴とする押出し機における押
出し制御装置。3. An extruder equipped with a measuring means for measuring the temperature controlled by the extruder, a measuring means for measuring the rubber temperature in the extrusion head, a measuring means for measuring the ambient temperature around the extruder, and a charging means. Measuring means for measuring the rubber temperature, rubber temperature in the extrusion head in the past stable state of extrusion, database for presetting and accumulating the screw rotation speed of the extruder and the speed of the take-up conveyor for this rubber temperature, and the extruder temperature The temperature control unit, the rubber temperature in the extruder head, the ambient temperature around the extruder, and the arithmetic unit for performing arithmetic operations on the rubber temperature in the extrusion head in the past stable extrusion state, and the arithmetic unit and the screw of the extruder. An extrusion control device in an extruder, wherein a rotary drive motor and a drive motor of a take-up conveyor are connected.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7159568A JPH091638A (en) | 1995-06-26 | 1995-06-26 | Method and apparatus for controlling to extrude in extruder |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7159568A JPH091638A (en) | 1995-06-26 | 1995-06-26 | Method and apparatus for controlling to extrude in extruder |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH091638A true JPH091638A (en) | 1997-01-07 |
Family
ID=15696571
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7159568A Pending JPH091638A (en) | 1995-06-26 | 1995-06-26 | Method and apparatus for controlling to extrude in extruder |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH091638A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006192582A (en) * | 2005-01-11 | 2006-07-27 | Bridgestone Corp | Extrusion control method of composite extruder |
JP2006298636A (en) * | 2005-04-25 | 2006-11-02 | Bridgestone Corp | Conveyance conveyor controller and conveyance conveyor control method |
JP2013043350A (en) * | 2011-08-24 | 2013-03-04 | Sumitomo Rubber Ind Ltd | Method and control device for extrusion of unvulcanized rubber |
JP2013107288A (en) * | 2011-11-21 | 2013-06-06 | Bridgestone Corp | Extruding train and extruding method |
JP2016002660A (en) * | 2014-06-13 | 2016-01-12 | 横浜ゴム株式会社 | Extrusion control method of rubber extruded product |
-
1995
- 1995-06-26 JP JP7159568A patent/JPH091638A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006192582A (en) * | 2005-01-11 | 2006-07-27 | Bridgestone Corp | Extrusion control method of composite extruder |
JP4535884B2 (en) * | 2005-01-11 | 2010-09-01 | 株式会社ブリヂストン | Extrusion control method for composite extruder |
JP2006298636A (en) * | 2005-04-25 | 2006-11-02 | Bridgestone Corp | Conveyance conveyor controller and conveyance conveyor control method |
JP4708842B2 (en) * | 2005-04-25 | 2011-06-22 | 株式会社ブリヂストン | Conveyor conveyor control device and conveyor method |
JP2013043350A (en) * | 2011-08-24 | 2013-03-04 | Sumitomo Rubber Ind Ltd | Method and control device for extrusion of unvulcanized rubber |
JP2013107288A (en) * | 2011-11-21 | 2013-06-06 | Bridgestone Corp | Extruding train and extruding method |
JP2016002660A (en) * | 2014-06-13 | 2016-01-12 | 横浜ゴム株式会社 | Extrusion control method of rubber extruded product |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2537089B2 (en) | Automatic greasing method for injection molding machine | |
JPH091638A (en) | Method and apparatus for controlling to extrude in extruder | |
JPH02204018A (en) | Method and apparatus of raising injection molding | |
JP2006321186A (en) | Rubber extruder and method of controlling variation of extruded rubber amount and transferred rubber amount | |
JP2786082B2 (en) | Automatic size change control system in inflation molding line | |
JPH05212773A (en) | Device for controlling emitting amount of extruder | |
JPH1086217A (en) | Film thickness control device in inflation molding process | |
JP3717556B2 (en) | Speed control device for striate coating line | |
JP2681590B2 (en) | Sheet width control method for extruded sheet material | |
JPH0815753B2 (en) | Film width control device | |
JP3180311B2 (en) | Apparatus for measuring the amount of material supplied to an extruder and an apparatus for controlling the discharge rate of the extruder using the same | |
SU1516372A1 (en) | Apparatus for manufacturing tyres by winding narrow strips | |
JP3610393B2 (en) | Extruder molding machine | |
JPH08156075A (en) | Controlling method of take-off speed of extrudate and device thereof | |
JPH04301427A (en) | Controller for continuous extrusion vulcanizing line | |
JPH1080947A (en) | Film thickness control device for inflation molding process | |
JP2024067182A (en) | Method and apparatus for producing rubber extrusion product | |
JPH10202724A (en) | Automatic wall thickness adjusting device in extrusion molding apparatus | |
JPH07285164A (en) | Calculation of extrusion amount of extruder for thermoplastic resin | |
JP2832387B2 (en) | Film width controller for inflation film manufacturing machine | |
JPH01275123A (en) | Size-changing system of formed object in inflation molding | |
JPH0825463A (en) | Extrusion molding method and apparatus | |
JPH05329916A (en) | Controlling device of multi-layered inflation film making machine | |
JPH071558A (en) | Extrusion control of strip like rubber material | |
JPH09300431A (en) | Slit gap adjusting device of cap, control of thickness of resin film and manufacture of resin film |