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JPH0657335B2 - Moisture content control device for coating machine - Google Patents
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JPH0657335B2 - Moisture content control device for coating machine - Google Patents

Moisture content control device for coating machine

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Publication number
JPH0657335B2
JPH0657335B2 JP63181162A JP18116288A JPH0657335B2 JP H0657335 B2 JPH0657335 B2 JP H0657335B2 JP 63181162 A JP63181162 A JP 63181162A JP 18116288 A JP18116288 A JP 18116288A JP H0657335 B2 JPH0657335 B2 JP H0657335B2
Authority
JP
Japan
Prior art keywords
moisture content
coating
feedforward signal
operation output
control device
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP63181162A
Other languages
Japanese (ja)
Other versions
JPH0231858A (en
Inventor
晴美 橋場
福井  聡
信章 橋本
匡 野口
一志 高野
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 Paper Mills Ltd
Yokogawa Electric Corp
Original Assignee
Mitsubishi Paper Mills Ltd
Yokogawa Electric Corp
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 Paper Mills Ltd, Yokogawa Electric Corp filed Critical Mitsubishi Paper Mills Ltd
Priority to JP63181162A priority Critical patent/JPH0657335B2/en
Publication of JPH0231858A publication Critical patent/JPH0231858A/en
Publication of JPH0657335B2 publication Critical patent/JPH0657335B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 <産業上の利用分野> 本発明は、塗工量制御装置における塗り出しスタート時
の水分率制御の制御性の改善に関する。
DETAILED DESCRIPTION OF THE INVENTION <Field of Industrial Application> The present invention relates to improvement of controllability of water content control at the start of coating in a coating amount control device.

<従来技術> 第3図により塗工制御装置の概要を説明する。1は原紙
ロール、2は塗工のために引き出された原紙、3は両面
の塗工が終了した紙2の巻取ロールである。
<Prior Art> An outline of a coating control device will be described with reference to FIG. Reference numeral 1 is a base paper roll, 2 is a base paper pulled out for coating, and 3 is a take-up roll of a paper 2 which has been coated on both sides.

4は紙2の一方の面に塗料を塗る第1塗工手段、5は塗
工前の紙の水分率と坪量を測定するための第1B/M
計、6は塗工手段4を経た紙を乾燥させるための第1ド
ライヤである。
4 is a first coating means for applying a paint to one surface of the paper 2, and 5 is a first B / M for measuring the moisture content and basis weight of the paper before coating.
A total of 6 is a first dryer for drying the paper which has passed through the coating means 4.

7はドライヤ6を経た紙2の他方の面に塗料を塗る第2
塗工手段、8は塗工前の紙の水分率と坪量を測定するた
めの第2B/M計、9は塗工手段4を経た紙を乾燥させ
るための第2ドライヤである。
7 is a second for applying paint to the other surface of the paper 2 that has passed through the dryer 6
A coating means, 8 is a second B / M meter for measuring the moisture content and basis weight of the paper before coating, and 9 is a second dryer for drying the paper which has passed through the coating means 4.

10は第3B/M計であり、第2ライヤ9を経た紙2の
水分率と坪量を測定する。
A third B / M meter 10 measures the moisture content and basis weight of the paper 2 that has passed through the second layer 9.

11は測定値演算手段であり、第1,第2,第3のB/
M計5,8,10の測定値M,M,Mを入力し
て、坪量と水分率に関する下流側の測定値と上流側の測
定値の差を演算し、第1塗工手段4による塗工量測定値
PV11とドライヤ6の出力側の水分率測定値PV12及び
第2塗工手段7による塗工量測定値PV12とドライヤ9
の出力側の水分率測定値PV22を出力する。これら測定
値に基づいて塗工量並びに水分率が目標設定値に制御さ
れる。
Reference numeral 11 is a measured value calculation means, which is the first, second, and third B /
The measured values M 1 , M 2 , and M 3 of the M meters 5, 8, and 10 are input to calculate the difference between the measured value on the downstream side and the measured value on the upstream side regarding the basis weight and the moisture content, and the first coating The coating amount measurement value PV 11 by the means 4, the moisture content measurement value PV 12 on the output side of the dryer 6, and the coating amount measurement value PV 12 by the second coating means 7 and the dryer 9
The measured moisture content value PV 22 on the output side is output. The coating amount and the water content are controlled to the target set values based on these measured values.

第4図は、塗工手段4及び第1ドライヤ6の拡大図であ
り、バッキングロール12により走行される紙2に対し
て、ファンテン13内の塗料14に下部が浸されたアプ
リケータロール15が上方に操作されて接触し、このア
プリケータロールを介して塗料が紙に付着され、付着塗
料の一部をブレード16により掻き落とすことにより塗
工量を制御する。17はフレードの角度を操作するアク
チュエータである。
FIG. 4 is an enlarged view of the coating means 4 and the first dryer 6, and the applicator roll 15 in which the lower portion is dipped in the paint 14 in the fan ten 13 with respect to the paper 2 run by the backing roll 12. Are operated to contact with each other, the paint is adhered to the paper through the applicator roll, and a part of the adhered paint is scraped off by the blade 16 to control the coating amount. Reference numeral 17 is an actuator for operating the angle of the flade.

水分率は、各ドライヤへの熱風供給量を操作することに
より制御される。18は第1ドライヤ6への熱風Hの供
給管路、19は供給量の制御弁、20は水分率調節計で
あって、水分率の測定値PV12と設定値SV12の偏差を
制御演算した操作出力MV12により制御弁19を操作す
る。
The moisture content is controlled by manipulating the amount of hot air supplied to each dryer. Reference numeral 18 is a supply line of the hot air H to the first dryer 6, 19 is a supply amount control valve, and 20 is a moisture content controller, which controls and calculates the deviation between the moisture content measured value PV 12 and the set value SV 12. operating the control valve 19 by the control output MV 12.

このような構成の塗工量制御装置における定常状態での
水分率制御の制御ループの一例を第1ドライヤ6につい
て第5図により説明する。DCSが制御装置側、Pがプ
ロセス側を示す。
An example of a control loop for controlling the water content in the steady state in the coating amount control device having such a configuration will be described with reference to FIG. 5 for the first dryer 6. DCS indicates the controller side, and P indicates the process side.

水分率調節計20の操作出力MV12は第1加算手段21
で第1フィードフォワード信号FFが加算され、更に
第2加算手段22で第2フィードフォワード信号FF
が加算され、これらフィードフォワード信号の加算操作
出力MV12′が制御弁19に供給される。
The operation output MV 12 of the moisture content controller 20 is the first addition means 21.
The first feedforward signal FF 1 is added by the second feedforward signal FF 2
Are added, and the addition operation output MV 12 ′ of these feedforward signals is supplied to the control valve 19.

23は第1フィードフォワード演算手段であり、塗工量
操作量MV11に基づいて塗工量操作に起因する水分率変
動の補償を実行する第1フィードフォワード信号FF
の変化量ΔFFを制御周期ごとに、 ΔFF=K・ΔMV11 (1) により演算して加算手段21に発信する。
Reference numeral 23 denotes a first feedforward calculation means, which is a first feedforward signal FF 1 for executing compensation of a water content variation caused by the coating amount operation based on the coating amount operation amount MV 11.
Change amount ΔFF 1 is calculated for each control cycle by ΔFF 1 = K 1 · ΔMV 11 (1) and transmitted to the adding means 21.

24は第2フィードフォワード演算手段であり、塗工前
の水分率測定値PV01に基づいて塗工量前の水分率変動
の補償を実行する第2フィードフォワード信号FF2の
変化量ΔFF2を制御周期ごとに、 ΔFF=−K(PV01n−PV01n-1) (2) により演算して加算手段22に発信する。
24 is a second feed-forward computing means, controlling the change amount ΔFF2 second feed-forward signal FF2 to perform compensation of coating quantity before the moisture content vary based on the moisture content measurements PV 01 before coating cycle For each time, ΔFF 2 = −K 2 (PV 01n −PV 01n−1 ) (2) is calculated and transmitted to the adding means 22.

調節計20の操作出力の変化量ΔMV12は、偏差をE
としたとき、 ΔMV12=100{(E−En-1)+E/T}/PB
(3) である、 従って、制御弁19への操作出力MV12′の変化量ΔM
12′は、 ΔMV12′=ΔFF+ΔFF+ΔMV12 (4) である。
The change amount ΔMV 12 of the operation output of the controller 20 is the deviation E n.
, ΔMV 12 = 100 {(E n −E n−1 ) + E n / T} / PB
(3) Therefore, the change amount ΔM of the operation output MV 12 ′ to the control valve 19 is
V 12 ′ is ΔMV 12 ′ = ΔFF 1 + ΔFF 2 + ΔMV 12 (4).

<発明が解決すべき問題点> このような構成により定常状態での水分率は塗工量操作
出力並びに塗工前の水分率変動がフィードフォワード補
償されて良好に制御されるが、塗工スタート時の水分率
の制御は、塗工スピードが変化している場合の塗工量変
化に対する適正な水分率制御が難しいために、過剰塗工
によるべた塗り(未乾燥)を避けるために、オペレータ
の手動介入により過乾燥となるように制御弁19へ一定
の操作出力を供給する運転を実行している。
<Problems to be solved by the invention> With such a configuration, the moisture content in the steady state is well controlled by feedforward compensation of the coating amount operation output and the moisture content variation before coating. It is difficult to control the water content at the time of application because it is difficult to control the water content appropriately when the coating speed changes, so to avoid solid coating (undried) due to excessive coating, The operation for supplying a constant operation output to the control valve 19 is performed so as to cause overdrying by manual intervention.

即ち、塗工スタート時は水分率の操作は一定の手動操作
で固定し、塗工量制御のみで立ち上げ、塗工量が安定し
てから定常制御に切換えている。
That is, when the coating is started, the water content is fixed by a fixed manual operation, the coating is started up only by controlling the coating amount, and the control is switched to the steady control after the coating amount is stabilized.

このために、スタート時におけるオペレータの操作が煩
雑で経験を要すると共に、スタート時の水分率の制御性
が悪いという問題点がある。
Therefore, there is a problem that the operator's operation at the start is complicated and requires experience, and the controllability of the water content at the start is poor.

本発明は、この様な問題点を解消できる塗工量制御装置
の提供を目的とする。
An object of the present invention is to provide a coating amount control device which can solve such problems.

<問題点を解決するための手段> このような目的を達成する本発明は、水分率センサの測
定値(PV)と水分率設定値(SV)の偏差を制御演算
した水分率操作出力(MV)により熱風ドライヤの操作
端を制御すると共に、塗工量操作出力に基づく第1フィ
ードフォワード信号(FF)並びに塗工前の水分率セ
ンサの測定値に基づく第2フィードフォワード信号(F
)を前記水分率操作出力に加算する塗工機の水分率
制御装置において、次の構成としたものである。
<Means for Solving Problems> In the present invention which achieves such an object, a moisture content operation output (MV) obtained by control calculation of a deviation between a moisture content sensor measured value (PV) and a moisture content set value (SV). ) Controls the operation end of the hot air dryer, and the first feedforward signal (FF 1 ) based on the coating amount operation output and the second feedforward signal (F 1 ) based on the measured value of the moisture content sensor before coating.
A water content control device for a coating machine that adds F 2 ) to the water content operation output has the following configuration.

即ち、塗工量センサの測定値に基づく第3フィードフォ
ワード信号(FF)を上記水分率操作出力に更に加算
する手段を設け、塗工スタート時において塗工スピード
が増速する場合は前記第3フィードフォワード信号の加
算を開始し、前記水分率センサの測定値が許容範囲内に
なると前記第3フィードフォワード信号の加算を遮断す
る切替え手段を設けたことを特徴としている。
That is, a means for further adding the third feedforward signal (FF 3 ) based on the measured value of the coating amount sensor to the above moisture content operation output is provided, and when the coating speed is increased at the start of coating, the above-mentioned first Switching means is provided for starting addition of the three feedforward signals and interrupting addition of the third feedforward signal when the measured value of the moisture content sensor falls within an allowable range.

<作用> 定常の運転状態では、塗工量操作出力に基づく第1フィ
ードフォワード信号並びに塗工前の水分率センサの測定
値に基づく第2フィードフォワード信号が水分率操作出
力に加算されている。そして、塗り始めの塗工スピード
が増速過程にある期間に限って、塗工量センサの測定値
に基づく第3フィードフォワード信号が水分率操作出力
に更に加算されるので、過渡的な運転状態でも紙質が目
標値に収束しやすくなる。
<Operation> In a steady operation state, the first feedforward signal based on the coating amount operation output and the second feedforward signal based on the measured value of the moisture rate sensor before coating are added to the moisture rate operation output. Then, the third feedforward signal based on the measured value of the coating amount sensor is further added to the moisture content operation output only during the period when the coating speed at the beginning of coating is in the process of increasing the speed, so that the transient operating state. However, the paper quality tends to converge to the target value.

<実施例> 第1図に基づいて本発明の実施例を説明する。第5図で
説明した要素と同一な要素についての説明は省略し、特
徴部についての説明を追加する。
<Example> An example of the present invention will be described with reference to FIG. Description of the same elements as those described in FIG. 5 will be omitted, and description of the characteristic portion will be added.

制御装置側において、25は第3加算手段であり、第3
フィードフォワード演算手段26よりのフィードフォワ
ード演算出力FFを調節計20の操作出力MVに加
算する。
On the control device side, 25 is a third adding means,
The feedforward calculation output FF 3 from the feedforward calculation means 26 is added to the operation output MV 2 of the controller 20.

また、第3フィードフォワード信号による塗工スピード
の影響補正が効果を上げて、水分率センサの測定値が許
容範囲内になると、第3フィードフォワード信号の加算
を遮断することにより、定常状態での制御状態に移行す
るので、第3フィードフォワード信号が定常状態の運転
に干渉することもない。
Further, when the effect correction of the coating speed by the third feedforward signal is effective and the measured value of the moisture content sensor is within the allowable range, the addition of the third feedforward signal is cut off, so that the steady state Since the control state is entered, the third feedforward signal does not interfere with the steady-state operation.

第3フィードフォワード演算手段26は、塗工量の測定
値PV11に基づいて、スピード変動による塗工量変動に
起因するスタート時の水分率変動の補償を実行するため
に、第3フィードフォワード信号FFの変化量ΔFF
3を制御周期ごとに、 ΔFF=KPV11n−PV11n-1) (5) により演算して加算手段25に発信する。
The third feedforward calculation means 26 executes the third feedforward signal FF in order to compensate the variation in the water content at the start due to the variation in the coating amount due to the variation in the speed, based on the measured coating amount PV11. Change amount of 2 ΔFF
ΔFF 3 = K 3 PV 11n −PV 11n−1 ) (5) is calculated for each control cycle and transmitted to the adding means 25.

従って、制御弁19への操作出力MV12′の変化量ΔM
12′は、(4)式にΔFFが追加されて、 ΔMV12′=ΔFF+ΔFF+ΔFF+ΔMV12 (6) である。
Therefore, the change amount ΔM of the operation output MV 12 ′ to the control valve 19
V 12 ′ is ΔMV 12 ′ = ΔFF 1 + ΔFF 2 + ΔFF 3 + ΔMV 12 (6) by adding ΔFF 3 to the equation (4).

27はシーケンス制御装置であり、塗工開始指令ST並
びにB/M計などの測定値が定常状態となる制御可フラ
グFLを受けて調節計20及び第1〜第3フィードフォ
ワード演算手段23,24,26に起動信号を発信す
る。
Reference numeral 27 is a sequence control device, which receives the coating start command ST and the controllable flag FL for which the measured values of the B / M meter and the like are in a steady state, and receives the controller 20 and the first to third feedforward calculation means 23, 24. , 26 to send a start signal.

第2図は動作の手順を示すフローチャート図である。先
ず、初期条件が満足された後、塗工開始指令により制御
可フラグが確認されるとタイマーTが起動されて一定
の待ち時間がおかれた後、水分率の偏差が一定の許容範
囲以上にある場合は、(6)式の演算による全操作出力
ΔMV12′による制御が実行され、水分率の偏差が許容
範囲内になると第3フィードフォワード信号FFの供
給を遮断して通常のフィードフォワード制御に移行す
る。
FIG. 2 is a flow chart showing the procedure of the operation. First, after the initial condition is satisfied, when the controllable flag is confirmed by the coating start command, the timer T 1 is started and a certain waiting time is set, and then the deviation of the water content exceeds a certain allowable range. In the case of, the control by the total operation output ΔMV 12 ′ by the calculation of the equation (6) is executed, and when the deviation of the water content is within the allowable range, the supply of the third feedforward signal FF 3 is cut off and the normal feed is performed. Move to forward control.

以上説明した実施例は、第1ドライヤ6側の制御の例で
あるが、第2ドライヤ9側についても同様に本発明を適
用することが可能である。
The embodiment described above is an example of control on the first dryer 6 side, but the present invention can be similarly applied to the second dryer 9 side.

<発明の効果> 以上説明したように、本発明によれば、塗工スタート時
におけるスピード変化に伴う塗工量変動に起因する水分
率変動を第3をフィードフォワード信号により適性に補
償することができ、塗り始めにおける水分率制御を自動
化することが可能となり、水分率制御の制御性を向上さ
せ、オペレータの負担、損紙の減少とエネルギーの節約
に貢献することができる。
<Effects of the Invention> As described above, according to the present invention, it is possible to appropriately compensate for the third fluctuation of the water content due to the fluctuation of the coating amount due to the speed change at the start of coating, by the feedforward signal. This makes it possible to automate the moisture content control at the beginning of coating, improve the controllability of the moisture content control, and contribute to the operator's burden, reduction of waste paper, and energy saving.

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

第1図は本発明の実施例を示す構成図、第2図は信号処
理の手順を示すフローチャート図、第3図は塗工機制御
装置の概念図、第4図は塗工手段並びにドライヤ部分の
拡大図、第5図は従来技術の一例を示す構成図である。 11……測定値演算手段、18……熱風供給管路、19
……制御弁、20……水分率調節計、21,22,25
……第1,第2,第3加算手段、23,24,26……
第1,第2,第3フィードフォワード信号演算手段、2
7……シーケンス制御装置
FIG. 1 is a configuration diagram showing an embodiment of the present invention, FIG. 2 is a flow chart diagram showing a signal processing procedure, FIG. 3 is a conceptual diagram of a coating machine control device, and FIG. 4 is a coating means and a dryer portion. FIG. 5 is a configuration diagram showing an example of a conventional technique. 11 ... Measured value calculating means, 18 ... Hot air supply pipe, 19
...... Control valve, 20 ...... Moisture content controller 21,22,25
...... First, second, third adding means, 23, 24, 26 ......
First, second, third feedforward signal calculation means, 2
7: Sequence control device

───────────────────────────────────────────────────── フロントページの続き (72)発明者 橋本 信章 青森県八戸市大字河原木字青森谷地3番地 三菱製紙株式会社八戸工場内 (72)発明者 野口 匡 東京都武蔵野市中町2丁目9番32号 横河 電機株式会社内 (72)発明者 高野 一志 東京都武蔵野市中町2丁目9番32号 横河 電機株式会社内 (56)参考文献 特開 昭63−54977(JP,A) 実公 昭61−40387(JP,Y2) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Nobuaki Hashimoto, Inventor No. 3 Aomori Yachi, Kawara Wood, Aomori Prefecture No. Yokogawa Electric Co., Ltd. (72) Inventor Kazushi Takano 2-9-32 Nakamachi, Musashino-shi, Tokyo Yokogawa Electric Co., Ltd. (56) References JP 63-54977 (JP, A) 61-40387 (JP, Y2)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】水分率センサの測定値(PV)と水分率設
定値(SV)の偏差を制御演算した水分率操作出力(M
V)により熱風ドライヤの操作端を制御すると共に、 塗工量操作出力に基づく第1フィードフォワード信号
(FF)並びに塗工前の水分率センサの測定値に基づ
く第2フィードフォワード信号(FF)を前記水分率
操作出力に加算する塗工機の水分率制御装置において、 塗工量センサの測定値に基づく第3フィードフォワード
信号(FF)を上記水分率操作出力に更に加算する手
段を設け、 塗工スタート時において塗工スピードが増速する場合は
前記第3フィードフォワード信号の加算を開始し、前記
水分率センサの測定値が許容範囲内になると前記第3フ
ィードフォワード信号の加算を遮断する切替え手段を設
けたことを特徴とする塗工機の水分率制御装置。
1. A moisture content operation output (M) obtained by control calculation of a deviation between a moisture content sensor measured value (PV) and a moisture content set value (SV).
V) controls the operation end of the hot air dryer, and also controls the first feedforward signal (FF 1 ) based on the coating amount operation output and the second feedforward signal (FF 2) based on the measurement value of the moisture content sensor before coating. ) Is added to the moisture content operation output, a means for further adding a third feedforward signal (FF 3 ) based on the measured value of the coating amount sensor to the moisture content operation output. When the coating speed is increased at the start of coating, the addition of the third feedforward signal is started, and when the measured value of the moisture content sensor is within the allowable range, the addition of the third feedforward signal is started. A water content control device for a coating machine, which is provided with a switching means for shutting off.
JP63181162A 1988-07-20 1988-07-20 Moisture content control device for coating machine Expired - Lifetime JPH0657335B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63181162A JPH0657335B2 (en) 1988-07-20 1988-07-20 Moisture content control device for coating machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63181162A JPH0657335B2 (en) 1988-07-20 1988-07-20 Moisture content control device for coating machine

Publications (2)

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JPH0231858A JPH0231858A (en) 1990-02-01
JPH0657335B2 true JPH0657335B2 (en) 1994-08-03

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2024172103A1 (en) 2023-02-16 2024-08-22 日本製鉄株式会社 Grooving method, grooving device, and grain-oriented electrical steel sheet

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6140387U (en) * 1984-08-18 1986-03-14 株式会社日立ホームテック Electric kotatsu packaging material
JPS6354977A (en) * 1986-08-26 1988-03-09 Yokogawa Electric Corp Method for controlling moisture content of coater

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2024172103A1 (en) 2023-02-16 2024-08-22 日本製鉄株式会社 Grooving method, grooving device, and grain-oriented electrical steel sheet

Also Published As

Publication number Publication date
JPH0231858A (en) 1990-02-01

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