JPS63133211A - Temperature control method for treating product - Google Patents

Temperature control method for treating product

Info

Publication number
JPS63133211A
JPS63133211A JP28115886A JP28115886A JPS63133211A JP S63133211 A JPS63133211 A JP S63133211A JP 28115886 A JP28115886 A JP 28115886A JP 28115886 A JP28115886 A JP 28115886A JP S63133211 A JPS63133211 A JP S63133211A
Authority
JP
Japan
Prior art keywords
product
temperature
meaning
processed product
conveyor
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.)
Granted
Application number
JP28115886A
Other languages
Japanese (ja)
Other versions
JP2512917B2 (en
Inventor
Hiromitsu Inoue
博光 井上
Ryoji Ito
伊藤 良二
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.)
Daido Steel Co Ltd
Original Assignee
Daido Steel 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 Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP61281158A priority Critical patent/JP2512917B2/en
Publication of JPS63133211A publication Critical patent/JPS63133211A/en
Application granted granted Critical
Publication of JP2512917B2 publication Critical patent/JP2512917B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Feedback Control In General (AREA)
  • Control Of Temperature (AREA)

Abstract

PURPOSE:To properly control the temperature of a treating product by detecting the passing time interval of the treating product to use this as an arithmetic element for both integration and differentiation terms. CONSTITUTION:A radiation thermometer 6 is set at a single side of a carry-in conveyor 4 corresponding to the transport downstream part of a treating conveyor 3 to measure the temperature of a treating product 1 together with a sensor 7 which detects the pass of the product 1. The temperature measurement signal of the product 1 obtained by the thermometer 6 is supplied to a microprocessor 8 together with the pass pulse signal of the product 1 obtained by the sensor 7. Then the processor 8 calculates the correction value DELTAPn by an equation including a 1st proportion term, a 2nd integration term and a 3rd differentiation term. Furthermore, Xn means the latest measured temperature of the product 1 in the equation together with Xn-1 and Xn-2 meaning the measured temperatures of the product 1 passed before a step and two steps, Rn meaning target temperature of the product 1, K meaning the proportion gain, T1 meaning the integration time, TD meaning the differentiation time, and tau meaning the passing time interval of the product 1. The value DELTAPn is converted by an inverter 9 into a signal that controls a variable speed motor 10 of the conveyor 3 and then supplied to the processor 8.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明はビレット状、塊状の処理品或いは自動車部品等
の単品状の処理品を連続的に所要温度に熱処理するもの
において、その処理品を搬送するコンベヤの運行速度を
制御することによりその処理温度を制御する方法に関す
るものである。
[Detailed Description of the Invention] [Industrial Field of Application] The present invention is a method for continuously heat-treating billet-like, block-like processed products, or single-processed products such as automobile parts to a required temperature. This invention relates to a method of controlling the processing temperature by controlling the speed of a conveyor.

[従来の技術と問題点コ 一般に冷却室或いは加熱室等の熱処理室を通過させるこ
とにより処理品を目標とする温度に冷却または加熱する
連続熱処理装置においては、従来からその処理品の搬送
速度を調節することにより該各処理品の熱処理室内の滞
在時間を変化させ該処理品の処理温度を制御することが
行なわれている。即ち、熱処理室の出口付近適宜個所に
処理品の温度を計る放射温度計等の温度計を設け、その
温度別による処理品の測定温度とその目標処理温度とを
比較し調節計を通しその偏差に応じて処理コンベヤの運
行速度を操作して処理品温度を目標処理温度に自動制御
するものが知られている。しかるに従来の方法は例えば
帯状材のように処理品が連続した形態のものでないと制
御系が期待どおり動作しない。即ち1例えば自動車エン
ジン用コンロッドのような単品状の処理品を処理コンベ
ヤ上に適当間隔を置いて次々と乗せて搬送し熱処理する
ような場合、特にその処理品間の間隔が不規則であると
上記従来の方法では一定周期でサンプリング(測温)す
るようにしたとしてもサンプリング時に処理品がその測
温位置に不在のこともあり適確なフィードバック信号が
得られないことから制御系がうまく動作しないおそれが
あった。
[Prior art and problems] Conventionally, in continuous heat treatment equipment in which the processed product is cooled or heated to a target temperature by passing through a heat treatment chamber such as a cooling chamber or a heating chamber, the transport speed of the processed product has traditionally been controlled. By adjusting the temperature, the residence time of each processed item in the heat treatment chamber is changed to control the processing temperature of the processed item. That is, a thermometer such as a radiation thermometer to measure the temperature of the processed product is installed at an appropriate location near the exit of the heat treatment chamber, and the measured temperature of the processed product at each temperature is compared with the target processing temperature, and the deviation is determined through a controller. There is a known system that automatically controls the temperature of processed products to a target processing temperature by operating the operating speed of a processing conveyor according to the processing speed. However, in the conventional method, the control system does not operate as expected unless the processed product is in a continuous form, such as a strip of material. In other words, 1. For example, when single products such as connecting rods for automobile engines are placed one after another on a processing conveyor at appropriate intervals and then transported and heat-treated, especially if the intervals between the products are irregular. In the conventional method described above, even if sampling (temperature measurement) is performed at regular intervals, the processed product may not be at the temperature measurement position at the time of sampling, and an accurate feedback signal cannot be obtained, so the control system does not work properly. There was a risk that it would not.

[問題点を解決するための手段] 本発明は上記問題点を解決するため、多数の単品状の処
理品が適当間隔を置いて処理コンベヤ上に乗せられて次
々と搬送されその搬送中に該処理品を冷却または加熱す
るものにおいて、処理コンベヤの搬送下流部における処
理品の温度を3する温度計を設けると共に該処理品の通
過を検知するセンサを設け、該処理コンベヤの運行速度
を次式によって与えられる修正量ΔPnによりフィード
バック制御することを特徴とした処理品の温度制御方法
を提供しようとするものである。
[Means for Solving the Problems] In order to solve the above-mentioned problems, the present invention provides a system in which a large number of single-piece processed products are placed on a processing conveyor at appropriate intervals and transported one after another, and during the transport, the In a device that cools or heats the processed product, a thermometer is installed to measure the temperature of the processed product downstream of the processing conveyor, and a sensor is installed to detect the passage of the processed product, and the operating speed of the processing conveyor is determined by the following formula: The present invention aims to provide a method for controlling the temperature of a processed product, which is characterized by performing feedback control using a correction amount ΔPn given by ΔPn.

[作用コ この式によって与えられる修正量ΔPnは処理品の通過
時間間隔が不定でそれを測温するサンプリング間隔が不
規則になったとしても適確なる3項動作(比例・積分・
微分)によるPID制御をなさしめることができる。
[Action] The correction amount ΔPn given by this equation is based on the three-term operation (proportional, integral,
(differential) PID control can be performed.

[実施例コ 次に図面に従い本発明の詳細な説明する。この実施例は
鍛造機によってプレスされた処理品1゜1・・・・を中
継用のコンベヤ2より自然空冷用の処理コンベヤ3に移
載し該処理コンベヤ3上を搬送される間に該処理品1,
1・・・・を自然放冷により所要温度に冷却させた後、
さらに該処理品1.1・・・・を装入用コンベヤ4に移
載し連続熱処理炉5に装入して鍛造時の歪取りを行なわ
しめるラインである。このラインでは鍛造機の作動間隔
が一定しないので処理品1.1・・・・は常に一定間隔
で送られて来るとは限らない。つまり処理コンベヤ3上
の処理品1,1・・・・間の間隔はランダムである。
[Example] Next, the present invention will be described in detail with reference to the drawings. In this embodiment, processed products 1゜1... pressed by a forging machine are transferred from a relay conveyor 2 to a processing conveyor 3 for natural air cooling, and are processed while being conveyed on the processing conveyor 3. Item 1,
1. After cooling to the required temperature by natural cooling,
Furthermore, this line transfers the treated products 1.1, . In this line, the operating intervals of the forging machines are not constant, so the processed products 1.1... are not always sent at regular intervals. In other words, the intervals between the processed products 1, 1, . . . on the processing conveyor 3 are random.

しかして該処理コンベヤ3の搬送下流部に当る装入用コ
ンベヤ4の一側に処理品1,1・・・・の温度を計る放
射温度計6を設けると共に5該処理品1゜1・・・・の
通過を検知するセンサ7を設ける。温度計6によって計
811された処理品の測定温度信号およびセンサ7から
得られた処理品通過のパルス43号はPID演算をなす
マイクロプロセッサ8に入力される。そして該マイクロ
プロセッサ8は下記修正量ΔPnを演算する。
Therefore, a radiation thermometer 6 for measuring the temperature of the processed products 1, 1, etc. is provided on one side of the charging conveyor 4, which is downstream of the processing conveyor 3. A sensor 7 is provided to detect the passage of... The temperature signal measured by the thermometer 6 and the pulse No. 43 obtained from the sensor 7 are input to the microprocessor 8 which performs a PID calculation. Then, the microprocessor 8 calculates the following correction amount ΔPn.

−Xn−2)は微分項である。-Xn-2) is a differential term.

このΔPnを与える式■はアナログ調節計の理想化され
た3項動作の制御式として知られている(To:微分時
間             jこの式から誘導される
差分形PID制御式は、Pn=KCLen +Σ−Th
en−1−P−(en   en−+  )ト・■にな
る。これを操作端の位置の修正量ΔPnを与える速度形
に変換するには上記式■を微分して、−−2en−+ 
+en−z )・・・・・・・・■この式に、err 
= Rn −Xn+ en−+ = Rn −Xn −
+en −2= Rn −Xn−2を代入することによ
って上記式■が誘導される。
The formula (■) giving this ΔPn is known as a control formula for the idealized three-term operation of an analog controller (To: differential time j) The differential PID control formula derived from this formula is Pn=KCLen +Σ- Th
en-1-P-(en en-+) becomes .■. To convert this into a velocity form that gives the correction amount ΔPn for the position of the operating end, differentiate the above equation (■) and calculate -2en-+
+en-z)・・・・・・・・・■In this formula, err
= Rn −Xn+ en−+ = Rn −Xn −
By substituting +en -2=Rn -Xn-2, the above formula (2) is derived.

しかして本発明にて用いられる式■の積分項ゲリング時
間即ち処理品の通過時間間隔7が分子と分母に夫々加重
要素として加えられ、積分項では偏差の持続した時間を
、微分項では偏差変動の時間的割合をもその要素として
夫々処理品が通過する度に演算される。そして弐〇によ
って与えられる修正量ΔPnはインバータ9にて処理コ
ンベヤ3の可変速モータ10を制御する信号に変換され
、該処理コンベヤ3の運行速度を修正制御し該処理コン
ベヤ3上の処理品1,1・・・・の搬送速度をコントロ
ールし放冷時間を調節することによってその搬送下流部
における該処理品1,1・・・・の温度を目標温度に自
動制御し、連続熱処理炉5に装入される際の該処理品1
.1・・・・の温度を一定ならしめる。
Therefore, the integral term Gelling time in formula (2) used in the present invention, that is, the transit time interval 7 of the processed product, is added as a weighting element to the numerator and denominator, respectively, and the integral term is the time during which the deviation lasted, and the differential term is the deviation change. The time ratio is also calculated each time a processed product passes through. The correction amount ΔPn given by 2〇 is converted into a signal for controlling the variable speed motor 10 of the processing conveyor 3 by the inverter 9, and the operating speed of the processing conveyor 3 is corrected and the processed products 1 on the processing conveyor 3 are controlled. , 1... by controlling the conveyance speed and adjusting the cooling time to automatically control the temperature of the treated products 1, 1... at the downstream part of the conveyance to the target temperature, and then transfer them to the continuous heat treatment furnace 5. The processed product 1 when being charged
.. 1. Keep the temperature constant.

なおこの時間7は放射温度計6の直前に設けたセンサ7
によって検知できるが、該センサは処理品の通過を検知
できれば必ずしもこの位置でなくともよい。
Note that this time 7 is the sensor 7 installed just before the radiation thermometer 6.
However, the sensor does not necessarily have to be in this position as long as it can detect the passage of the processed product.

このように本発明は処理品の通過時間間隔を積分項ゲイ
ンと微分項ゲインの要素として加重するものであるので
、サンプリング周期が一定でなくても積分項、微分項が
異常な値となることがない。
In this way, the present invention weights the passing time interval of the processed product as an element of the integral term gain and the differential term gain, so even if the sampling period is not constant, the integral term and the differential term will have abnormal values. There is no.

[発明の効果] 以上実施例について説明したように本発明に係る処理品
の制御方法は、処理品の通過時間間隔を検知しこれを積
分項および微分項の演算要素とすることにより処理品の
通過間隔が不規側で測温サンプリングが一定間隔で行な
えなくても、比例項と積分項と微分項による3項動作の
理想的な制御特性が常に達成され処理品の温度を適格に
制御できる有益なものである。
[Effects of the Invention] As described above with respect to the embodiments, the method for controlling the processed product according to the present invention detects the passing time interval of the processed product and uses this as a calculation element for the integral term and the differential term. Even if the passing interval is irregular and temperature measurement sampling cannot be performed at regular intervals, the ideal control characteristics of three-term operation using the proportional, integral, and differential terms are always achieved and the temperature of the processed product can be properly controlled. It is beneficial.

4、図面は本発明の一実施例を示した処理品の連続熱処
理装置の温度制御系統図である。
4. The drawing is a temperature control system diagram of a continuous heat treatment apparatus for processed products showing an embodiment of the present invention.

l・・・・処理品、3・・・・処理コンベヤ、6・・・
・温度計、7・・・・通過検知センサ、8・・・・マイ
クロプロセッサ、9・・・・インバータ、lO・・・・
可変速モータ。
l...Processing product, 3...Processing conveyor, 6...
・Thermometer, 7... Passage detection sensor, 8... Microprocessor, 9... Inverter, lO...
Variable speed motor.

Claims (1)

【特許請求の範囲】 多数の単品状の処理品が適当間隔を置いて処理コンベヤ
上に乗せられて次々と搬送されその搬送中に該処理品を
冷却または加熱するものにおいて、処理コンベヤの搬送
下流部における処理品の温度を計る温度計を設けると共
に該処理品の通過を検知するセンサを設け、該処理コン
ベヤの運行速度を次式によって与えられる修正量ΔPn
によりフィードバック制御することを特徴とした処理品
の温度制御方法。 ΔPn=K(Xn_−_1−Xn)+(K・τ/T_I
)(Rn−Xn)+(K・T_D)/τ(2Xn_−_
1−Xn−Xn_−_2)〔ただし Xn;処理品の最新の測定温度 Xn_−_1;1つ前に通過した処理品の測定温度Xn
_−_2;2つ前に通過した処理品の測定温度Rn;処
理品の目標処理温度 K;比例ゲイン(定数) T_I;積分時間(定数) T_D;微分時間(定数) τ;処理品の通過時間間隔〕
[Scope of Claims] In an apparatus in which a large number of single products to be processed are placed on a processing conveyor at appropriate intervals and conveyed one after another, and the processed products are cooled or heated during the conveyance, the downstream part of the processing conveyor is A thermometer is provided to measure the temperature of the processed product in the section, and a sensor is provided to detect the passage of the processed product, and the operating speed of the processing conveyor is adjusted by the correction amount ΔPn given by the following equation.
A method for controlling the temperature of a processed product, characterized by feedback control. ΔPn=K(Xn_-_1-Xn)+(K・τ/T_I
)(Rn-Xn)+(K・T_D)/τ(2Xn_-_
1-Xn-Xn_-_2) [However, Xn: Latest measured temperature of processed product
____2; Measured temperature Rn of the processed product that passed two times ago; Target processing temperature K of the processed product; Proportional gain (constant) T_I; Integral time (constant) T_D; Derivative time (constant) τ; Passage of the processed product Time interval〕
JP61281158A 1986-11-26 1986-11-26 Temperature control method for processed products Expired - Lifetime JP2512917B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61281158A JP2512917B2 (en) 1986-11-26 1986-11-26 Temperature control method for processed products

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61281158A JP2512917B2 (en) 1986-11-26 1986-11-26 Temperature control method for processed products

Publications (2)

Publication Number Publication Date
JPS63133211A true JPS63133211A (en) 1988-06-06
JP2512917B2 JP2512917B2 (en) 1996-07-03

Family

ID=17635163

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61281158A Expired - Lifetime JP2512917B2 (en) 1986-11-26 1986-11-26 Temperature control method for processed products

Country Status (1)

Country Link
JP (1) JP2512917B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100529549B1 (en) * 1998-12-28 2006-01-27 삼성전자주식회사 Remote control circuit for semiconductor equipment
JP2006130226A (en) * 2004-11-09 2006-05-25 Shigenobu Takane Evacuation appliance

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5354105A (en) * 1976-10-27 1978-05-17 Sumitomo Metal Ind Ltd Heating temperature controlling method for strip
JPS596207U (en) * 1982-06-30 1984-01-14 横河電機株式会社 sample value controller
JPS61239310A (en) * 1985-04-16 1986-10-24 Hitachi Metals Ltd Temperature controller

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5354105A (en) * 1976-10-27 1978-05-17 Sumitomo Metal Ind Ltd Heating temperature controlling method for strip
JPS596207U (en) * 1982-06-30 1984-01-14 横河電機株式会社 sample value controller
JPS61239310A (en) * 1985-04-16 1986-10-24 Hitachi Metals Ltd Temperature controller

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100529549B1 (en) * 1998-12-28 2006-01-27 삼성전자주식회사 Remote control circuit for semiconductor equipment
JP2006130226A (en) * 2004-11-09 2006-05-25 Shigenobu Takane Evacuation appliance

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Publication number Publication date
JP2512917B2 (en) 1996-07-03

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