JPS63173621A - Control device for raising temperature of plastic sheet forming die - Google Patents

Control device for raising temperature of plastic sheet forming die

Info

Publication number
JPS63173621A
JPS63173621A JP62004031A JP403187A JPS63173621A JP S63173621 A JPS63173621 A JP S63173621A JP 62004031 A JP62004031 A JP 62004031A JP 403187 A JP403187 A JP 403187A JP S63173621 A JPS63173621 A JP S63173621A
Authority
JP
Japan
Prior art keywords
temperature
value
die
control
loop
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
JP62004031A
Other languages
Japanese (ja)
Inventor
Toshiaki Iida
飯田 俊彰
Kosuke Onaka
康祐 尾中
Seishi Shi
師 清史
Toshimi Murayama
利美 村山
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.)
Mitsubishi Heavy Industries Ltd
Konica Minolta Inc
Original Assignee
Mitsubishi Heavy Industries Ltd
Konica Minolta Inc
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 Mitsubishi Heavy Industries Ltd, Konica Minolta Inc filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP62004031A priority Critical patent/JPS63173621A/en
Publication of JPS63173621A publication Critical patent/JPS63173621A/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
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/30Extrusion nozzles or dies
    • B29C48/305Extrusion nozzles or dies having a wide opening, e.g. for forming sheets
    • 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
    • B29C2948/92504Controlled 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

Landscapes

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

Abstract

PURPOSE:To form a sheet excellent in accuracy, and free of warps of lip gap due to temperature difference by raising the temperature of a sheet forming die, while regulating said temperature at small steps with a specified set temperature control device. CONSTITUTION:The thermostat 31 of remotely and locally set type and the temperature signal generator 32 of remotely set type are attached to a sheet forming die 5. Die temperatures T1-Tn of each loop are read out with the temperature signal generator 32 of remotely set type, and the process treatment corresponding to said temperature is carried out, thereby outputting a remotely set temperature signal TS and a set mood command signal. The temperature control outputs the temperature value added with a shaft temperature t, while waiting the elapse of a specified time (t) to each thermostat 31, as a new set value to uniform the temperature in the die 5 by conduction, after the temperature of total loop has reached, an initially set value. While repeating this process, if the temperature reaches final temperature Tf in the temperature raising process, the set mood command signal S is cut, and the sheet is formed by ordinary temperature control.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は押出成形機用シート成形ダイの温度制御方法に
利用できるプラスチックシート成形ダイの昇温制御方法
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for controlling the temperature increase of a plastic sheet molding die, which can be used as a temperature control method for a sheet molding die for an extrusion molding machine.

(従来の技術) 第4図に従来のプラスチックシート成形ダイにおける温
度制御装置の1例を示す。図においてダイ5の温度制御
は、同ダイ5の巾方向に分割された複数のループから成
り、各ループの制御機器はヒータ1、測温素子2、温度
調節計3、ヒータ電力調節器4より構成されている。
(Prior Art) FIG. 4 shows an example of a temperature control device in a conventional plastic sheet molding die. In the figure, the temperature control of the die 5 consists of multiple loops divided in the width direction of the die 5, and the control equipment for each loop is a heater 1, a temperature measuring element 2, a temperature controller 3, and a heater power regulator 4. It is configured.

さて第4図における制御方法としては、温度調節計3に
て設定値(設定器は温度調節計3に内蔵)と測温素子2
から送られたダイ温度とを比較した後、その偏差を制御
演算し、この結果を出力としてヒータ電力調節器4へ送
る。ヒータ電力調節器4では、前記調節計3の出力信号
値に応じて、ヒータ1への供給電力を調節し、グイ温度
が設定値になる様制御する。
Now, as for the control method in Fig. 4, the temperature controller 3 sets the set value (the setting device is built in the temperature controller 3) and the temperature measuring element 2
After comparing the temperature with the die temperature sent from the controller, the deviation is controlled and calculated, and the result is sent to the heater power regulator 4 as an output. The heater power regulator 4 adjusts the power supplied to the heater 1 according to the output signal value of the controller 3, and controls the goo temperature to a set value.

また設定温度は、当初から生産運転時の目標温度にセッ
トして昇温する方法が一般的で、設定値と実測値に偏差
の存在する昇温途中では、ヒータ1は100%の能力で
ダイ5を加熱することになる。また第4図から分る様に
、各ループは相互の関連は全く無く、独立した個別の制
御を行っている。
In addition, the set temperature is generally set to the target temperature during production operation from the beginning and then raised. During the temperature rise when there is a deviation between the set value and the actual measured value, the heater 1 operates at 100% capacity. 5 will be heated. Further, as can be seen from FIG. 4, each loop has no relation to each other and performs independent and individual control.

(発明が解決しようとする問題点) 前記第4図の装置では、ダイ5は樹脂流路等内部構造が
複雑なため、各制御ループ相当部のダイ熱容量と、それ
ぞれのヒータ加熱能力との比を一定に設計することは極
めて困難で、現実にはかなりのバラツキが存在する。と
ころが前記の通り、各制御ループが相互の温度に無関係
に、それぞれ100%能力で加熱するため、昇温速度に
差を生じ、各ループ相当のダイ間に温度ムラを生じる。
(Problems to be Solved by the Invention) In the device shown in FIG. 4, the die 5 has a complicated internal structure such as the resin flow path, so the ratio between the die heat capacity of the portion corresponding to each control loop and the heating capacity of each heater is It is extremely difficult to design a constant value, and in reality there is considerable variation. However, as described above, since each control loop heats at 100% capacity regardless of the temperature of each other, a difference occurs in the temperature increase rate, resulting in temperature unevenness between dies corresponding to each loop.

また同一ループのダイ各部についても、急加熱するため
、ヒータ密着部と内部とでは温度差を生じることになる
Further, since each part of the die in the same loop is heated rapidly, a temperature difference occurs between the part in close contact with the heater and the inside.

一方、ダイ5はプラスチックシート6の厚みプロファイ
ルが目標通り押し出し得る様、分解清掃後の組立時、リ
ップゲージを使用して巾方向のリップ隙間を精密に調整
している。ところが、昇温中に前記の温度ムラを生じる
と、熱膨張差により調整したリップ隙間パターンに狂い
を生じ、運転開始後、シート6を押し出しながら再調整
行う必要があり、スタートアップ時の製品歩留りが悪く
なるなどの問題があった。またある制御ループのヒータ
が断線しているような場合では、ダイ内温度にアンバラ
ンスを生じ、ダイに悪影響をおよぼす虞れがあった。
On the other hand, the lip gap in the width direction of the die 5 is precisely adjusted using a lip gauge during assembly after disassembly and cleaning so that the thickness profile of the plastic sheet 6 can be extruded as desired. However, if the above-mentioned temperature unevenness occurs during temperature rise, the adjusted lip gap pattern will be distorted due to the difference in thermal expansion, and it will be necessary to readjust the lip gap pattern while pushing out the sheet 6 after the start of operation, which will reduce the product yield at startup. There were problems such as deterioration. Furthermore, if a heater in a certain control loop is disconnected, there is a possibility that the temperature inside the die will be unbalanced, which may adversely affect the die.

本発明は前記従来の問題点を解決するために提案された
ものである。
The present invention has been proposed to solve the above-mentioned conventional problems.

(問題点を解決するための手段及び作用)このため本発
明は、プラスチックシート成形グイの昇温制御方法にお
いて、ダイの巾方向に分割された複数の温度制御ループ
の設定値を共通の値とし、その共通設定値は制御開始時
の各ループ計測値中の最小値、又は最小値に微小温度を
加えた値を初期値として昇温を始め、全ループが設定値
に到達したのを確認後、あるいは更に一定時間経過後に
、その設定値に角度微小温度加算した値を新たな設定値
として昇温を継続すると共に、前記の各作動を繰返すこ
とにより、微小ステップ状に徐々に温度を上げ、予め設
定された昇温終了温度に到達したら、各ループ個別の設
定値による制御に切換えることにより、グイ内部の温度
分布を均一に保ちながら昇温を可能にするようにしたも
ので、これを問題点解決のための手段及び作用とするも
のである。
(Means and effects for solving the problem) For this reason, the present invention provides a temperature increase control method for a plastic sheet molding die, in which the setting values of a plurality of temperature control loops divided in the width direction of the die are set to a common value. , the common set value is the minimum value of each loop measurement value at the start of control, or the value obtained by adding a minute temperature to the minimum value as the initial value, and the temperature begins to rise, and after confirming that all loops have reached the set value. Or, after a certain period of time has elapsed, the value obtained by adding the angular minute temperature to the set value is set as a new set value, and the temperature continues to rise, and the temperature is gradually raised in minute steps by repeating each of the above operations, When the preset heating end temperature is reached, control is switched to the individual setting values for each loop, making it possible to raise the temperature while keeping the temperature distribution inside the goo uniform. It is a means and action for point-solving.

(実施例) 以下本発明の1実施例を図面について説明すると、第1
図は本発明の実施例を示すプラスチックシート成形ダイ
の昇温制御装置を示す。なお、第1図において1はヒー
タ、2は測温素子、4はヒータ電力調節器、5はダイで
あり、これらは第4図の従来と同一のため、ここではこ
れらの詳細な説明は省略する。
(Embodiment) Below, one embodiment of the present invention will be explained with reference to the drawings.
The figure shows a temperature increase control device for a plastic sheet molding die showing an embodiment of the present invention. In addition, in FIG. 1, 1 is a heater, 2 is a temperature measuring element, 4 is a heater power regulator, and 5 is a die, and since these are the same as the conventional device shown in FIG. 4, detailed explanations of these are omitted here. do.

さて第1図において第4図に示した従来の方式との相違
点は、温度調節計3に代えて、リモート、ローカル設定
式温度調節計31を採用して、温度設定がリモート、ロ
ーカルの何れも可能であり、そしてその切換えを外部か
らの信号により行い得るタイプを使用することと、リモ
ート設定温度信号発生器32を設けてなる2点にある。
Now, the difference between FIG. 1 and the conventional system shown in FIG. There are two points: using a type that can perform the switching by an external signal, and providing a remote setting temperature signal generator 32.

ここでローカル設定とは、温度調節計内蔵の設定器によ
るものであり、またリモート設定とは、外部の装置から
信号を与える設定方式である。
Here, local setting refers to a setting device with a built-in temperature controller, and remote setting refers to a setting method in which a signal is applied from an external device.

次にり°モート設定温度信号発生器32について説明す
ると、このリモート設定温度信号発生器32は、各ルー
プのダイ温度T□〜T、を読み取り、その温度に応じて
第2図に示す演算処理を行って、各温度調節計32へ前
述の共通設定値となるべきリモート設定温度信号T、と
、設定モード指令信号Sを出力する。
Next, to explain the remote set temperature signal generator 32, this remote set temperature signal generator 32 reads the die temperature T□~T of each loop, and performs the calculation process shown in FIG. 2 according to the temperature. Then, the remote setting temperature signal T, which should be the common setting value mentioned above, and the setting mode command signal S are output to each temperature controller 32.

次に第2図、第3図に基づき昇温動作制御の作用を説明
する。制御スタート指令により、リモート設定温度信号
T3をイニシャライズすると共に、設定モード指令信号
SをONとし、各温度調節計31をリモートモードに切
換える。次に測温素子2の信号、即ち各部のダイ温度T
i〜T7を読み取り、その中から最低温度Tm1nを選
択し、その値へ微小温度へTを加算した値をリモート設
定温度信号T3として、各温度調節計31へ出力する。
Next, the effect of temperature increase operation control will be explained based on FIGS. 2 and 3. The control start command initializes the remote setting temperature signal T3, turns on the setting mode command signal S, and switches each temperature controller 31 to the remote mode. Next, the signal of the temperature measuring element 2, that is, the die temperature T of each part
i to T7 are read, the lowest temperature Tm1n is selected from among them, and the value obtained by adding T to that value to the minute temperature is output to each temperature controller 31 as a remote set temperature signal T3.

ダイ5の各温度制御ループは、この値を初期設定値とし
て昇温を開始する。
Each temperature control loop of the die 5 starts increasing the temperature using this value as an initial setting value.

そしてしばらく経過して全ループの温度がこの値に到達
したら、ダイ5内の温度が伝導により均一化するための
一定時間tの経過を待ち、更に微小温度△Tを加算した
値を新たな設定値として各温度調節計31へ出力する。
After a while, when the temperature of all the loops reaches this value, wait for a certain time t to equalize the temperature inside the die 5 by conduction, and then set a new value by adding the minute temperature △T. It is output as a value to each temperature controller 31.

これを逐次繰返すことにより、設定信号T、は、第3図
に示す如く階段状に徐々に変化し、昇温終了温度T、に
到達したら、設定モード指令信号SをOFFにして温度
調節計31をローカルモードに切換え、各ループ単独の
通常の温度制御に入り、生産運転開始の状態となる。な
お、前記△T。
By repeating this process, the setting signal T gradually changes in a stepwise manner as shown in FIG. switches to local mode, enters normal temperature control for each loop individually, and enters the state of starting production operation. Note that the above △T.

Tt、を及び各温度調節計31のローカル設定値は、制
御スタート前に予め設定しておくものである。
Tt and the local setting values of each temperature controller 31 are set in advance before starting the control.

また制御開始時の各ループ計測値の最小値を初期値とし
て昇温を開始してもよい。
Alternatively, the temperature increase may be started using the minimum value of each loop measurement value at the start of control as an initial value.

本発明の主眼は均一な昇温であるが、下記の特長も併せ
持っている。即ち、リモート設定値の初期値は、前記の
如く制御スタート時の最小計測値から自動的に決定され
るため、昇温途中でヒータ断線、漏電等のトラブルによ
り一旦中断し、再昇温する場合でも、自動的に温度ギャ
ップを生じない設定値が得られ、効率的な昇温が可能で
ある。また昇温途中でヒータ断線したような場合でも、
そこで昇温動作が止るため、温度のアンバランスによる
ダイへの悪影響が回避できる。
Although the main focus of the present invention is uniform temperature rise, it also has the following features. In other words, the initial value of the remote setting value is automatically determined from the minimum measured value at the start of control as described above, so if heating is interrupted due to a problem such as heater disconnection or electric leakage during heating, and then heating is restarted. However, it is possible to automatically obtain a set value that does not cause a temperature gap, allowing efficient temperature rise. Also, even if the heater breaks during temperature rise,
Since the temperature increase operation stops at this point, adverse effects on the die due to temperature imbalance can be avoided.

(発明の効果) 以上詳細に説明した如く本発明のシート成形ダイの昇温
制御方法は、全ループ同一般定値で、かつ全てのループ
が設定値へ到達したのを確認しながら、微小ステップ状
に設定値を上げるため、ダイ内部に温度ムラを生ずるこ
となく、均一な温度で昇温が可能である。従って熱膨張
差にょろりツブ隙間に狂いを生じることなく、運転当初
から目標プロフィールに近い、精度の良いシートが得ら
れる。
(Effects of the Invention) As explained in detail above, the method for controlling the temperature increase of a sheet forming die according to the present invention is to control the temperature rise in a microstep manner while keeping all loops at the same general fixed value and confirming that all loops have reached the set value. Since the set value is raised to , it is possible to raise the temperature uniformly without causing temperature unevenness inside the die. Therefore, a highly accurate sheet that is close to the target profile can be obtained from the beginning of operation without causing deviations in the lug gaps due to thermal expansion differences.

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

第1図は本発明の実施例を示すプラスチックシート成形
ダイの昇温制御装置のシステム図、第2図は第1図に記
載のリモート設定温度信号発生器の演算処理フローダイ
ヤグラム、第3図は本発明における共通設定値(リモー
ト設定温度信号)の変化を示す線図、第4図は従来のプ
ラスチックシート成形ダイの温度制御装置のシステム図
である。 図の主要部分の説明 1−ヒータ       2−・測温素子4−・ヒータ
電力調節器  5・−ダイ6−プラスチックシート 3l−IJモート、ローカル設定式温度調節計32−I
Jモート設定温度信号発生器 亮2図 第3図 箆4図
FIG. 1 is a system diagram of a temperature increase control device for a plastic sheet molding die showing an embodiment of the present invention, FIG. 2 is a calculation processing flow diagram of the remote setting temperature signal generator shown in FIG. 1, and FIG. FIG. 4, which is a diagram showing changes in the common set value (remote set temperature signal) in the present invention, is a system diagram of a conventional temperature control device for a plastic sheet molding die. Explanation of the main parts of the diagram 1 - Heater 2 - Temperature measuring element 4 - Heater power regulator 5 - Die 6 - Plastic sheet 3l - IJ mote, local setting type temperature controller 32 - I
J-Mote setting temperature signal generator Ryo 2 Fig. 3 Fig. 4

Claims (1)

【特許請求の範囲】[Claims] プラスチックシート成形ダイの昇温制御方法において、
ダイの巾方向に分割された複数の温度制御ループの設定
値を共通の値とし、その共通設定値は制御開始時の各ル
ープ計測値中の最小値、又は最小値に微小温度を加えた
値を初期値として昇温を始め、全ループが設定値に到達
したのを確認後、あるいは更に一定時間経過後に、その
設定値に角度微小温度加算した値を新たな設定値として
昇温を継続すると共に、前記の各作動を繰返すことによ
り、微小ステップ状に徐々に温度を上げ、予め設定され
た昇温終了温度に到達したら、各ループ個別の設定値に
よる制御に切換えることにより、ダイ内部の温度分布を
均一に保ちながら昇温を可能にしたことを特徴とするプ
ラスチックシート成形ダイの昇温制御方法。
In the temperature rise control method of plastic sheet molding die,
The set value of multiple temperature control loops divided in the width direction of the die is set as a common value, and the common set value is the minimum value of each loop measurement value at the start of control, or the value obtained by adding a minute temperature to the minimum value. Start heating with the initial value as the initial value, and after confirming that all loops have reached the set value, or after a certain period of time has passed, continue heating with the value added to the set value as the angular minute temperature as the new set value. At the same time, by repeating each of the above operations, the temperature is gradually raised in minute steps, and when the preset heating end temperature is reached, the temperature inside the die is increased by switching to control using the individual set values for each loop. A temperature increase control method for a plastic sheet molding die, which is characterized by making it possible to increase temperature while maintaining uniform distribution.
JP62004031A 1987-01-13 1987-01-13 Control device for raising temperature of plastic sheet forming die Pending JPS63173621A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62004031A JPS63173621A (en) 1987-01-13 1987-01-13 Control device for raising temperature of plastic sheet forming die

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62004031A JPS63173621A (en) 1987-01-13 1987-01-13 Control device for raising temperature of plastic sheet forming die

Publications (1)

Publication Number Publication Date
JPS63173621A true JPS63173621A (en) 1988-07-18

Family

ID=11573590

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62004031A Pending JPS63173621A (en) 1987-01-13 1987-01-13 Control device for raising temperature of plastic sheet forming die

Country Status (1)

Country Link
JP (1) JPS63173621A (en)

Similar Documents

Publication Publication Date Title
JPS635401A (en) Proportional control method for program temperature regulator
KR20130007965A (en) Control apparatus and control method
JPH0872115A (en) Temperature control method for injection molding machine
CN109483842A (en) A kind of control method and system of injection molding machine staged heating and heat preservation
JP6058180B1 (en) Temperature control device for manufacturing equipment
US6861018B2 (en) Temperature control method and apparatus for injection molding structure
JPH06180613A (en) Heating temperature controller
JPS63173621A (en) Control device for raising temperature of plastic sheet forming die
JP4533337B2 (en) Temperature control method for injection molding machine
JPS6260252B2 (en)
JP3779057B2 (en) Zone division heater temperature control device
WO1999040497A1 (en) Temperature controller for zone division heater
JPH11345030A (en) Temperature controller for heater devided into zones
JP2597920B2 (en) Temperature control method for injection molding machine
JPH01127121A (en) Mold temperature controller
JPH056102Y2 (en)
JP2002127220A (en) Method for controlling heating of gate for multi-cavity mold
WO2016142991A1 (en) Temperature control system and temperature control method
JPH02259806A (en) Controller
JP2002160276A (en) Method for controlling nozzle temperature of injection molding machine and nozzle temperature control device
JPH11115012A (en) Temperature controller of injection mold
JPH01180318A (en) Control method of automatic temperature-rise for extrusion machine
JPH10109343A (en) Mold temperature control method and apparatus therefor
JPH1158481A (en) Method for controlling temperature in heater for injection molding machine
JPH071509A (en) Method and device for regulating temperature of nozzle of injection device