Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0126751B2 - - Google Patents
[go: Go Back, main page]

JPH0126751B2 - - Google Patents

Info

Publication number
JPH0126751B2
JPH0126751B2 JP17827380A JP17827380A JPH0126751B2 JP H0126751 B2 JPH0126751 B2 JP H0126751B2 JP 17827380 A JP17827380 A JP 17827380A JP 17827380 A JP17827380 A JP 17827380A JP H0126751 B2 JPH0126751 B2 JP H0126751B2
Authority
JP
Japan
Prior art keywords
film thickness
coating
signal
nip pressure
coater
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
Application number
JP17827380A
Other languages
Japanese (ja)
Other versions
JPS57102266A (en
Inventor
Yoshasu Terasaka
Masao Tanabe
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.)
Chugai Ro Co Ltd
Original Assignee
Chugai Ro 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 Chugai Ro Co Ltd filed Critical Chugai Ro Co Ltd
Priority to JP17827380A priority Critical patent/JPS57102266A/en
Publication of JPS57102266A publication Critical patent/JPS57102266A/en
Publication of JPH0126751B2 publication Critical patent/JPH0126751B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Coating Apparatus (AREA)

Description

【発明の詳細な説明】 本発明は連続塗装ラインにおける塗膜厚制御装
置および塗膜厚制御方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a coating film thickness control device and a coating film thickness control method in a continuous coating line.

連続塗装ラインにおいては、塗膜厚を一定に保
持する必要がある。
In a continuous coating line, it is necessary to maintain a constant coating thickness.

従来、一般に、塗膜厚の制御は、手動によりコ
ータロールのギヤツプを調整することにより行な
われている。
Conventionally, coating film thickness has generally been controlled by manually adjusting the gap of a coater roll.

しかしながら、この方法では、せいぜい±3ミ
クロン程度の塗膜厚の設定しかできず、膜厚ムラ
が大きく、また膜厚が安全側に設定されるため、
それだけ塗料を多量に消費するという欠点および
塗装位置と膜厚測定位置が異なるため制御が安定
しないという欠点があつた。
However, with this method, it is only possible to set a coating thickness of about ±3 microns at most, and the coating thickness is large, and the coating thickness is set on the safe side.
This method has disadvantages in that it consumes a large amount of paint, and in that control is unstable because the coating position and the film thickness measurement position are different.

本発明者等は、前記自動化について種々検討し
たところ、塗膜厚検出器からの同一信号であつて
も、塗料条件、原板条件、ロール条件等により、
塗膜厚が変化するという事実を見出した。
The present inventors have conducted various studies regarding the above-mentioned automation, and have found that even if the signal from the coating film thickness detector is the same, it may vary depending on paint conditions, original plate conditions, roll conditions, etc.
It was discovered that the coating film thickness changes.

本発明は前記事実に鑑みて、塗膜厚検出器から
の信号を、塗料条件、原板条件、前処理条件等に
基ずいて予め実測して入力してある函数の中から
条件に適合する函数を選び出すデータ処理器と、
該函数に対応した信号を可変ムダ時間制御し、つ
いで、塗料条件と操業条件の実測データに基ずい
て求めた函数から操作用の設定出力を取り出す演
算器とにより演算し、塗膜厚を制御するようにし
た連続塗装ラインにおける塗膜厚制御装置および
塗膜厚制御方法を提供しようとするものである。
In view of the above facts, the present invention converts the signal from the coating film thickness detector into a function that satisfies the conditions from among functions that have been actually measured and inputted in advance based on paint conditions, original plate conditions, pre-processing conditions, etc. a data processor that selects the
The signal corresponding to the function is controlled for variable waste time, and then calculated by a calculator that extracts the setting output for operation from the function determined based on the actual measurement data of the paint conditions and operating conditions to control the paint film thickness. It is an object of the present invention to provide a coating film thickness control device and a coating film thickness control method in a continuous coating line.

つぎに、本発明を一実施例にしたがつて説明す
る。
Next, the present invention will be explained according to one embodiment.

第1図は本発明のフローシートを示し、第2図
は赤外線塗膜厚検出器1の機構を示す。赤外線塗
膜厚検出器1は、塗装乾燥されて連続的に搬送さ
れてくる塗装原板Wに赤外線発生器9から赤外線
を照射し、この赤外線が塗膜厚により選択吸収さ
れ、原板W表面で反射されて入力してくる減衰量
を赤外線センサー部10で測定し、塗膜信号を取
り出す。
FIG. 1 shows a flow sheet of the present invention, and FIG. 2 shows the mechanism of the infrared coating thickness detector 1. The infrared coating film thickness detector 1 irradiates infrared rays from an infrared generator 9 to a painted original plate W that has been dried and is continuously conveyed, and this infrared ray is selectively absorbed depending on the coating thickness and reflected on the surface of the original plate W. The infrared sensor unit 10 measures the amount of attenuation inputted by the infrared ray sensor 10, and extracts a coating film signal.

ついで、この塗膜信号をリニアライザ2で直線
化しA/D変換する。そして、この膜厚信号を膜
厚データ処理器3に入力する。
Next, this coating film signal is linearized by a linearizer 2 and A/D converted. This film thickness signal is then input to the film thickness data processor 3.

データ処理器3には塗料の種類、原板の種類お
よび前処理条件等に基ずいて膜厚信号と膜厚との
関係を函数に表わしたものがそれぞれ多数の条件
について入力されている。そして、運転開始前
に、これらの条件を設定することにより、その条
件に適合した函数が選択される。ついで、前記膜
厚信号が入力すると、前記函数に従つて補正ある
いは係数を求めることによつて真の膜厚信号を取
り出す。
A function representing the relationship between a film thickness signal and film thickness based on the type of paint, the type of original plate, preprocessing conditions, etc. is input to the data processor 3 for a large number of conditions. By setting these conditions before starting operation, a function that meets the conditions is selected. Then, when the film thickness signal is input, the true film thickness signal is extracted by correcting or determining a coefficient according to the function.

中央演算器4には、この膜厚信号を可変ムダ時
間制御および設定膜厚との偏差を演算する可変ム
ダ時間制御部5と、演算部6とを備えている。
The central processing unit 4 includes a variable waste time control section 5 and a calculation section 6, which perform variable waste time control on the film thickness signal and calculate the deviation from the set film thickness.

なお、可変ムダ時間制御部5は操作信号により
コータを制御して新しい条件で塗布した位置が測
定部に達するまでの時間をラインスピードから算
出し、その時間、操作部を制御しないよう可変の
空白時間を設けるものであり、新しい条件の塗布
位置を測定したとき、前記と同様に指令と指令と
の間に空白時間を持つて制御するものである。
The variable wasted time control unit 5 controls the coater using operation signals, calculates the time required for the coated position under new conditions to reach the measurement unit from the line speed, and sets a variable blank time so that the operation unit is not controlled during that time. When the coating position under new conditions is measured, control is performed by providing a blank time between commands in the same way as described above.

演算部6は、塗料の組成、希釈率等の塗料条件
および原板の速度、ロール硬度等の操業条件に基
ずいて前記膜厚信号とコータ操作用の設定出力と
の関係を函数化したものをそれぞれ多数の条件に
ついて入力している。
The calculation unit 6 converts the relationship between the film thickness signal and the set output for coater operation into a function based on paint conditions such as paint composition and dilution rate, and operating conditions such as original plate speed and roll hardness. A large number of conditions are entered for each.

そして前記塗料条件と操業条件が予め設定され
ると、その条件に対応した函数が選択される。つ
いで膜厚信号が入力すると、選択されている函数
関係および前記設定膜厚との偏差とからコータ操
作用の設定出力が取り出される。この場合、操業
条件が変更されないときは、何も条件を変えなく
てもよいことは言うまでもない。
Once the paint conditions and operating conditions are set in advance, a function corresponding to the conditions is selected. Then, when a film thickness signal is input, a set output for coater operation is extracted from the selected functional relationship and the deviation from the set film thickness. In this case, it goes without saying that if the operating conditions are not changed, there is no need to change any conditions.

ロールギヤツプまたはニツプ圧ドライバ7は前
記設定出力に基ずいてロールギヤツプまたはニツ
プ圧を制御する駆動機構8を操作する出力信号を
出力する。この操作信号がニツプ力またはロール
ギヤツプ駆動機構8に入力され、コータロール回
転数およびロールギヤツプを精度よく数値制御す
るものである。
The roll gap or nip pressure driver 7 outputs an output signal for operating a drive mechanism 8 for controlling the roll gap or nip pressure based on the set output. This operation signal is inputted to the nip force or roll gap drive mechanism 8 to accurately numerically control the coater roll rotation speed and roll gap.

以上の説明で明らかなように、本発明によれ
ば、膜厚検出器からの信号を、フイードバツクの
みでコータロール回転数およびロールギヤツプに
変換するのではなく、実測値に基ずいた各種の要
因および条件をフイードバツク値に対応させて各
駆動機構の操作出力信号としている。なお、前記
膜厚データ処理器、中央演算器等を一台の演算器
に組み込むこともできる。しかし、可変ムダ時間
制御部により、新しい条件で塗布た位置が塗膜厚
検出器に達するまで駆動機構の制御を持つため、
設定膜厚を±0.5〜1ミクロン程度の精度で簡単
な設備で自動制御することが可能となつた。
As is clear from the above explanation, according to the present invention, the signal from the film thickness detector is not converted into the coater roll rotation speed and roll gap only by feedback, but is converted into the coater roll rotation speed and roll gap based on various factors and The conditions are made to correspond to the feedback values and are used as operation output signals for each drive mechanism. Note that the film thickness data processor, central processing unit, etc. can also be incorporated into one processing unit. However, the variable wasted time control section controls the drive mechanism until the coating position reaches the coating thickness detector under the new conditions.
It has become possible to automatically control the set film thickness with an accuracy of about ±0.5 to 1 micron using simple equipment.

したがつて、使用塗料が削減でき、かつ、製品
の均一化を図ることができる。
Therefore, the amount of paint used can be reduced and the product can be made more uniform.

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

第1図は本発明にかかるフローシートで、第2
図は赤外線塗膜厚検出器である。 1…赤外線塗膜厚検出器、2…リニアライザ、
3…膜厚データ処理器、4…中央演算器、5…可
変ムダ時間制御部、6…演算部、7…ロールギヤ
ツプまたはニツプ圧ドライバ、8…駆動機構。
Figure 1 is a flow sheet according to the present invention;
The figure shows an infrared coating thickness detector. 1...Infrared coating thickness detector, 2...Linearizer,
3... Film thickness data processor, 4... Central computing unit, 5... Variable waste time control section, 6... Arithmetic section, 7... Roll gap or nip pressure driver, 8... Drive mechanism.

Claims (1)

【特許請求の範囲】 1 赤外線の選択吸収と反射とにより塗膜厚を検
出する赤外線塗膜厚検出器と、塗料の種類、原板
前処理条件等に基ずいて予め入力している塗膜信
号と膜厚との関係を函数化したものから膜厚信号
を取り出すデータ処理器と、該膜厚信号と設定膜
厚とを比較して制御位置と塗装位置との時間的ず
れをなくす制御を行なうとともに、塗料の種類に
基ずいて予め入力されている操業条件に適合した
設定出力を出すコータ制御演算器と、該コータ制
御演算器からの操作信号によりコータロールの回
転数およびロールギヤツプまたはニツプ圧を数値
調整する各駆動機構とから構成したことを特徴と
する連続塗装ラインにおける塗膜厚制御装置。 2 コータ制御演算器に設定膜厚または膜厚を入
力し、現在操業中の塗料の種類、原板前処理条件
等に適合したロールニツプ圧設定出力を取り出
し、この設定出力をニツプ圧ドライバに入力する
とともに、実際に測定したロールニツプ圧と比較
し、これらの値が一致するようにロールニツプ圧
駆動機構を数値制御することにより塗膜厚を制御
することを特徴とする連続塗装ラインにおける塗
膜厚制御方法。
[Claims] 1. An infrared coating thickness detector that detects coating thickness by selective absorption and reflection of infrared rays, and a coating signal that is input in advance based on the type of paint, original plate pretreatment conditions, etc. A data processor extracts a film thickness signal from a function obtained by converting the relationship between the film thickness and the film thickness, and performs control to eliminate the time lag between the control position and the painting position by comparing the film thickness signal and the set film thickness. In addition, there is a coater control calculator that outputs a setting output that matches the operating conditions input in advance based on the type of paint, and a control signal that controls the rotation speed of the coater roll and the roll gap or nip pressure based on operation signals from the coater control calculator. A coating film thickness control device for a continuous coating line, characterized by comprising drive mechanisms for numerical adjustment. 2. Input the set film thickness or film thickness into the coater control calculator, take out the roll nip pressure setting output that matches the type of paint currently in operation, original plate pretreatment conditions, etc., and input this setting output into the nip pressure driver. A method for controlling coating film thickness in a continuous coating line, characterized in that the coating thickness is controlled by comparing the actually measured roll nip pressure and numerically controlling a roll nip pressure drive mechanism so that these values match.
JP17827380A 1980-12-16 1980-12-16 Controller for paint film thickness in continuous painting line Granted JPS57102266A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17827380A JPS57102266A (en) 1980-12-16 1980-12-16 Controller for paint film thickness in continuous painting line

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17827380A JPS57102266A (en) 1980-12-16 1980-12-16 Controller for paint film thickness in continuous painting line

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP16407384A Division JPS6064664A (en) 1984-08-03 1984-08-03 Film thickness control method in coating line

Publications (2)

Publication Number Publication Date
JPS57102266A JPS57102266A (en) 1982-06-25
JPH0126751B2 true JPH0126751B2 (en) 1989-05-25

Family

ID=16045585

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17827380A Granted JPS57102266A (en) 1980-12-16 1980-12-16 Controller for paint film thickness in continuous painting line

Country Status (1)

Country Link
JP (1) JPS57102266A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116770395B (en) * 2023-08-22 2023-10-20 深圳市互成自动化设备有限公司 Electrophoretic powder spraying coating quality monitoring method and system

Also Published As

Publication number Publication date
JPS57102266A (en) 1982-06-25

Similar Documents

Publication Publication Date Title
US4766966A (en) Apparatus and method of controlling rate of feeding product to weigher
US3819948A (en) Method and apparatus for controlling the quantity of oil coated on continuously moving material
US11980966B2 (en) Method, computer program and laser cutting system for smart corner cutting
US3930774A (en) Extruder controller
JPH0126751B2 (en)
US3930922A (en) Process control
GB2046900A (en) Method of controlling the thickness of a moving web
JP3659292B2 (en) Coating thickness control method, coating thickness control apparatus, and pressure-sensitive adhesive tape manufactured using this method
JPH0323225B2 (en)
JPS63128199A (en) Method for controlling the thickness of treated coatings on surface-treated materials
JPS6124082B2 (en)
JPH0471593B2 (en)
JPH01186208A (en) Automatic plate thickness control device for rolling mill
JPS63130205A (en) Method for controlling thickness of tapered metal plate
KR102679773B1 (en) Control system of tandem cold rolling mill
JPH05185022A (en) Method for directly applying resin on metallic sheet
JPS6445613A (en) Method for controlling thickness of rubber sheet
JPS5645206A (en) Compensational controller for eccentricity of roll of rolling mill
JPS6216811A (en) Method for correcting phase delay of roll eccentricity control
JPS61222618A (en) Adaptive controlling method in rolling mill
JP3473785B2 (en) Resin thickness profile control device and resin coating method for resin coating machine
JPS57140667A (en) Method and apparatus for thickness control of applied paint film
JPS5794368A (en) Automatic controller for paint film thickness of painted strip manufacturing facility
SU1416582A1 (en) Apparatus for automatic control of process parameter ,particularly, moisture content of paper web
JPH07115000B2 (en) Coating thickness control method