JPH059796A - Electrodeposition coating method and device - Google Patents
Electrodeposition coating method and deviceInfo
- Publication number
- JPH059796A JPH059796A JP16463091A JP16463091A JPH059796A JP H059796 A JPH059796 A JP H059796A JP 16463091 A JP16463091 A JP 16463091A JP 16463091 A JP16463091 A JP 16463091A JP H059796 A JPH059796 A JP H059796A
- Authority
- JP
- Japan
- Prior art keywords
- electrodeposition
- coating
- temperature
- coated
- voltage
- 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.)
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Abstract
(57)【要約】
【目的】 自動的に塗装条件を判断し制御することによ
って、塗装品質を向上する。
【構成】 コンベア5によって搬送される被塗物4を認
識手段6によって認識し、予め定める時間内の総被塗物
面積を演算手段28によって算出する。前記予め定める
時間内の電流および電圧と、前記総被塗物面積とから塗
膜固有抵抗を算出し、塗膜固有抵抗とつきまわり性との
関係から電着塗料の制御液温を算出し、電着塗料液温を
制御する。
(57) [Summary] [Purpose] To improve the coating quality by automatically judging and controlling the coating conditions. [Structure] The coating object 4 conveyed by the conveyor 5 is recognized by the recognition means 6, and the total coating material area within a predetermined time is calculated by the calculation means 28. The current and voltage within the predetermined time, and the coating film resistivity is calculated from the total area to be coated, and the control liquid temperature of the electrodeposition coating composition is calculated from the relationship between the coating film resistivity and throwing power, Controls the temperature of electrodeposition paint liquid.
Description
【0001】[0001]
【産業上の利用分野】本発明は、電着塗料を用いて塗装
を行う電着塗装方法および装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrodeposition coating method and apparatus for coating with an electrodeposition coating.
【0002】[0002]
【従来の技術】従来から塗装方法としては、静電塗装方
法やスプレ塗装方法、エアーレス塗装方法やディッピン
グ塗装方法および電着塗装方法などが行われている。こ
のうち、電着塗装方法は、残余の塗装方法に比較してさ
まざまな面で優れた特徴を有しており、たとえば被塗物
の袋状構造部および被塗物の各部分間の接合部などにお
いても塗装が可能であるという特徴を有している。ま
た、上述のような特徴点に加え、通電量の制御などによ
ってつきまわり性の管理も容易であり、しかも塗装され
た塗料の「タレ」、「ワキ」なども発生せず、作業性が
良好であることが知られている。2. Description of the Related Art Conventionally, as a coating method, an electrostatic coating method, a spray coating method, an airless coating method, a dipping coating method, an electrodeposition coating method and the like have been performed. Among them, the electrodeposition coating method has excellent characteristics in various aspects as compared with the rest of the coating methods. For example, the bag-shaped structure portion of the article to be coated and the joint portion between each portion of the article to be coated. It also has the feature that it can be painted. In addition to the features described above, it is easy to control throwing power by controlling the amount of electricity, etc. Moreover, there is no "dripping" or "armpits" in the applied paint, and workability is good. Is known to be.
【0003】[0003]
【発明が解決しようとする課題】上述したようなつきま
わり性は、一般に通電電圧で制御されるが、他の要因、
たとえば塗膜固有抵抗、塗料液温、被塗物の搬送速度、
塗料内に浸漬されている被塗物数、塗料制御などにも影
響を受ける。すなわち、一定の電圧下で塗装を行ってい
ても、塗装面積が変動したり、塗膜固有抵抗が変動した
り、または塗料性状の変化などによって、塗膜が形成さ
れにくくなる場合があり、このような場合、塗料膜厚が
薄くなってしまい、被塗物の防錆性能が低下し、得られ
た製品が早期に発錆して機械的強度の低下や、外観を損
ねる事態となってしまう。The throwing power as described above is generally controlled by the applied voltage, but other factors,
For example, coating resistivity, coating liquid temperature, transfer speed of the coated object,
It is also affected by the number of objects to be dipped in the paint and paint control. That is, even if the coating is performed under a constant voltage, the coating area may change, the coating film resistivity may change, or the coating property may change, so that the coating film may not be formed easily. In such a case, the paint film thickness will be reduced, the anticorrosion performance of the object to be coated will deteriorate, and the resulting product will rust early and the mechanical strength will deteriorate and the appearance will be impaired. .
【0004】また、前記塗膜がむやみに厚く形成されて
しまう条件となった場合、塗料をむやみに消費して経済
性が悪化してしまう。さらに、塗装膜厚がむやみに増大
することによって、仕上がり外観や品質が悪化してしま
うという問題点がある。Further, under the condition that the coating film is formed unnecessarily thick, the paint is consumed unnecessarily and the economical efficiency is deteriorated. Further, there is a problem that the finish appearance and quality are deteriorated due to the excessive increase of the coating film thickness.
【0005】この従来技術では、塗料性状の変動および
塗膜固有抵抗の変動などを自動的に検出して、前記電圧
を自動制御するようには構成されていないため、膜厚の
正確な管理ができず、また稼働中の塗装条件の変動に対
応できないという問題点を有している。This prior art is not configured to automatically detect a change in paint property and a change in coating film specific resistance and automatically control the voltage, so that the film thickness can be accurately controlled. There is a problem in that it is not possible to cope with fluctuations in coating conditions during operation.
【0006】本発明の目的は、上述の問題点を解決し、
塗装品質が格段に向上されるとともに、そのための制御
を自動的に行うことができる電着塗装方法および装置を
提供することである。The object of the present invention is to solve the above-mentioned problems,
It is an object of the present invention to provide an electrodeposition coating method and apparatus capable of significantly improving coating quality and automatically controlling the coating quality.
【0007】[0007]
【課題を解決するための手段】本発明は、電着塗料が収
容された電着槽内に被塗物を搬送し、この被塗物と電着
槽内に貯留されている電極との間に直流電源を接続し、
電着塗装を行う電着塗装方法において、前記電源の電流
と電圧と、さらに被塗物の塗装面積とを検出し、前記電
流と電圧と塗装面積との間に演算を施して塗膜固有抵抗
を求め、前記塗膜固有抵抗と予め定めるつきまわり性と
のパラメータに対応する電着塗料の液温を算出し、前記
液温となるように塗料の温度を変化し、これによってつ
きまわり性を制御することを特徴とする電着塗装方法で
ある。SUMMARY OF THE INVENTION According to the present invention, an article to be coated is conveyed into an electrodeposition tank containing an electrodeposition coating material, and between the article to be coated and an electrode stored in the electrodeposition tank. Connect the DC power supply to
In the electrodeposition coating method for performing electrodeposition coating, the current and voltage of the power source, and further the coating area of the object to be coated are detected, and the coating film specific resistance is calculated by performing calculation between the current, voltage and coating area. Then, the liquid temperature of the electrodeposition coating material corresponding to the parameters of the coating film specific resistance and the predetermined throwing power is calculated, and the temperature of the coating is changed so as to reach the liquid temperature. It is an electrodeposition coating method characterized by controlling.
【0008】また本発明は、前記電着塗料液温は、塗膜
固有抵抗とつきまわり性とをパラメータとする予め定め
た係数を求め、前記係数と電着槽内の電着塗料の温度と
を演算して求めることを特徴とする。Further, in the present invention, the temperature of the electrodeposition coating solution is determined by a predetermined coefficient using the coating film resistivity and throwing power as parameters, and the coefficient and the temperature of the electrodeposition coating material in the electrodeposition tank are calculated. Is calculated and obtained.
【0009】また本発明は、電着塗料を収容する電着槽
と、被塗物を電着槽内に搬送して浸漬する搬送手段と、
電着槽内に設けられる電極と、被塗物と電極との間に電
力を供給する電源と、前記電源の電流を検出する電流検
出手段と、前記電源の電圧を検出する電圧検出手段と、
被塗物の塗装面積を表す信号を導出する塗装面積信号発
生手段と、電流検出手段と電圧検出手段と塗装面積信号
発生手段との各出力に応答し、塗膜固有抵抗を演算する
第1演算手段と、つきまわり性を表す信号を導出するつ
きまわり性信号導出手段と、電着槽内の電着塗料の温度
を検出する温度検出手段と、電着槽内の電着塗料の温度
を上昇または下降する熱交換器と、第1演算手段とつき
まわり性信号導出手段との各出力に応答し、塗膜固有抵
抗とつきまわり性と電着塗料の温度とを演算して目標液
温を求める第2演算手段と、第2演算手段の出力に応答
して電着槽内の電着塗料が前記目標液温になるように、
前記熱交換器を制御する制御手段とを含むことを特徴と
する電着塗装装置である。The present invention further comprises an electrodeposition tank for containing the electrodeposition coating material, and a transfer means for transferring and immersing the object to be coated in the electrodeposition tank.
An electrode provided in the electrodeposition tank, a power supply for supplying electric power between the object to be coated and the electrode, a current detection means for detecting a current of the power supply, a voltage detection means for detecting a voltage of the power supply,
A first calculation for calculating the coating film specific resistance in response to each output of the coating area signal generating means for deriving a signal representing the coating area of the object to be coated, the current detecting means, the voltage detecting means and the coating area signal generating means. Means, a throwing power signal deriving means for deriving a signal indicating throwing power, a temperature detecting means for detecting the temperature of the electrodeposition paint in the electrodeposition tank, and a temperature rise of the electrodeposition paint in the electrodeposition tank Alternatively, in response to each output of the descending heat exchanger, the first calculation means and the throwing power signal deriving means, the coating film specific resistance, throwing power and the temperature of the electrodeposition paint are calculated to obtain the target liquid temperature. A second computing means to be obtained and, in response to the output of the second computing means, so that the electrodeposition paint in the electrodeposition tank reaches the target liquid temperature,
An electrodeposition coating apparatus comprising: a control unit that controls the heat exchanger.
【0010】[0010]
【作用】本発明に従えば、電着塗料が収容された電着槽
内に被塗物を搬送し、この被塗物と電着槽内に貯留され
ている電極との間に直流電源を接続し、浸漬して電着塗
装を行う電着塗装方法において、先ず前記電流と電圧
と、さらに被塗物の塗装面積とが検出される。前記電流
と電圧と塗装面積との間に演算を施して塗膜固有抵抗を
求め、塗膜固有抵抗と予め定めるつきまわり性とのパラ
メータに対応する電着塗料の液温が算出される。前記液
温となるように塗料の温度を変化し、これによってつき
まわり性が制御される。According to the present invention, the object to be coated is conveyed into the electrodeposition tank containing the electrodeposition coating material, and a DC power supply is provided between the object to be coated and the electrode stored in the electrodeposition tank. In the electrodeposition coating method of connecting and dipping to perform electrodeposition coating, first, the current and voltage, and further the coating area of the object to be coated are detected. An arithmetic operation is performed among the current, the voltage and the coating area to obtain the coating film specific resistance, and the liquid temperature of the electrodeposition coating composition corresponding to the parameters of the coating film specific resistance and the predetermined throwing power is calculated. The temperature of the paint is changed so as to reach the liquid temperature, and the throwing power is controlled by this.
【0011】また本発明に従えば、塗膜固有抵抗とつき
まわり性とをパラメータとする予め定めた係数を求め、
前記係数と電着槽内の電着塗料の温度とを演算すること
によって、電着塗料の液温が求められる。Further, according to the present invention, a predetermined coefficient having the coating film resistivity and throwing power as parameters is calculated,
By calculating the coefficient and the temperature of the electrodeposition paint in the electrodeposition tank, the liquid temperature of the electrodeposition paint can be obtained.
【0012】また本発明に従えば、電着塗装装置は、電
着塗料を収容する電着槽と、被塗物を電着槽内に搬送し
て浸漬する搬送手段と、電着槽内に設けられる電極と、
被塗物と電極との間に電力を供給する電源と、前記電源
の電流を検出する電流検出手段と、前記電源の電圧を検
出する電圧検出手段と、被塗物の塗装面積を表す信号を
導出する塗装面積信号発生手段と、電流検出手段と電圧
検出手段と塗装面積信号発生手段との各出力に応答して
塗膜固有抵抗を演算する第1演算手段と、つきまわり性
を表す信号を導出するつきまわり性信号導出手段と、電
着槽内の電着塗料の温度を検出する温度検出手段と、電
着槽内の電着塗料の温度を上昇または下降する熱交換器
と、第1演算手段とつきまわり性信号導出手段との各出
力に応答し、塗膜固有抵抗とつきまわり性と電着塗料の
温度とを演算して目標液温を求める第2演算手段と、第
2演算手段の出力に応答して電着槽内の電着塗料が前記
目標液温になるように前記熱交換器を制御する制御手段
とを含む。According to the present invention, the electrodeposition coating apparatus includes an electrodeposition tank for containing an electrodeposition coating material, a transfer means for transferring and immersing an object to be coated in the electrodeposition tank, and an electrodeposition tank in the electrodeposition tank. An electrode provided,
A power supply for supplying electric power between the object to be coated and the electrode, a current detecting means for detecting the current of the power source, a voltage detecting means for detecting the voltage of the power source, and a signal representing the coating area of the object to be coated. A coating area signal generating means for deriving, a first calculating means for calculating a coating film specific resistance in response to each output of the current detecting means, the voltage detecting means and the coating area signal generating means, and a signal representing the throwing power. A throwing power signal deriving means for deriving, a temperature detecting means for detecting the temperature of the electrodeposition coating material in the electrodeposition tank, a heat exchanger for raising or lowering the temperature of the electrodeposition coating material in the electrodeposition vessel; Second computing means for responding to the outputs of the computing means and the throwing power signal deriving means to obtain the target liquid temperature by computing the coating film specific resistance, throwing power and the temperature of the electrodeposition paint, and second computing means. In response to the output of the means, the electrodeposition paint in the electrodeposition tank reaches the target liquid temperature. A and a control means for controlling the heat exchanger.
【0013】[0013]
【実施例】図1は本発明の一実施例である電着塗装装置
1を示す図であり、図2は図1に示される熱交換手段1
7を示す図である。電着槽2に電着塗料3が満たされて
おり、電着槽2上には被塗物4を搬送して電着塗料3に
被塗物4を浸漬できるような搬送手段であるコンベア5
が設置されている。コンベア5上の被塗物4が電着塗料
3に浸漬する前に、被塗物の認識手段6が設置されてい
る。認識手段6は、カメラからの映像信号に応答して被
塗物4の種類と台数とを認識する。被塗物4の種類毎の
塗装面積は、予め入力手段から後述する演算手段28に
入力されており、認識手段6によって認識された各種被
塗物4に対応した塗装面積と、各種被塗物4毎の台数と
の積の総和によって、電着槽2に浸漬された被塗物4の
表面積の合計値である総被塗物面積Sが求められる。1 is a view showing an electrodeposition coating apparatus 1 which is an embodiment of the present invention, and FIG. 2 is a heat exchange means 1 shown in FIG.
It is a figure which shows 7. The electrodeposition coating tank 3 is filled with the electrodeposition coating material 3, and the conveyor 5 which is a transfer means for transferring the coating object 4 on the electrodeposition tank 2 and dipping the coating object 4 in the electrodeposition coating material 3
Is installed. Before the article 4 to be coated on the conveyor 5 is dipped in the electrodeposition coating material 3, the recognition means 6 for the article to be coated is installed. The recognizing means 6 recognizes the type and the number of the objects to be coated 4 in response to the video signal from the camera. The coating area for each type of the coating object 4 is input in advance from the input means to the calculating means 28 described later, and the coating area corresponding to the various coating objects 4 recognized by the recognizing means 6 and the various coating objects. The total product area S, which is the total value of the surface areas of the objects 4 to be dipped in the electrodeposition tank 2, can be obtained by the sum of the products of the number of objects for each item 4.
【0014】顔料主体補給塗料槽9から顔料主体塗料が
ポンプ10によって流量計11を介して混合器12へ、
クリヤ主体補給塗料槽13からクリヤ主体塗料がポンプ
14によって流量計15を介して混合器12へ流入され
る。顔料主体塗料の主成分は顔料であり、他に樹脂や水
などを含んでいる。またクリヤ主体塗料には顔料は含ま
れておらず、樹脂や水などを含んでいる。The pigment-based paint is supplied from the pigment-based replenishment paint tank 9 to the mixer 12 via the flow meter 11 by the pump 10.
The clear-based paint is supplied from the clear-based replenishment paint tank 13 into the mixer 12 by the pump 14 via the flow meter 15. The main component of the pigment-based paint is a pigment, which additionally contains resin, water, and the like. Clear clear paint does not contain pigment, but contains resin and water.
【0015】混合器12には、さらに電着塗料3を抜出
して熱交換手段17で温度調整を行った電着塗料3およ
びポンプ18によって抜出された電着塗料3が混合され
て電着槽2に投入される。The mixer 12 is further mixed with the electrodeposition paint 3 extracted by the heat exchange means 17 and the electrodeposition paint 3 extracted by the pump 18, and the electrodeposition tank is prepared. It is thrown in 2.
【0016】図2は、図1に示される熱交換手段17を
示す図であり、図2(1)は熱交換を行わない場合の熱
交換手段17を示し、図2(2)は熱交換を行う場合の
熱交換手段17を示している。混合器12と電着槽2と
を結ぶ管路19と、冷却水が通る流路20とが熱交換器
21部分で接触している。流路20には、熱交換器21
の入口側と出口側とを結ぶバイパス流路22が形成され
ており、バイパス流路22の熱交換器21出口側には、
三方弁23が設けられている。三方弁23は後述するよ
うに演算手段28に接続されており、演算手段28は、
三方弁23を制御して、電着塗料3の液温を降下させる
場合には冷却水を熱交換器21に通し、降下させない場
合には冷却水をバイパス流路22に通すことによって温
度調節を行う。FIG. 2 is a view showing the heat exchange means 17 shown in FIG. 1. FIG. 2 (1) shows the heat exchange means 17 when heat exchange is not performed, and FIG. 2 (2) is heat exchange. The heat exchange means 17 for performing is shown. A pipe line 19 connecting the mixer 12 and the electrodeposition tank 2 and a flow passage 20 through which the cooling water passes are in contact with each other at a heat exchanger 21 portion. A heat exchanger 21 is provided in the flow path 20.
Is formed on the outlet side of the heat exchanger 21 of the bypass passage 22.
A three-way valve 23 is provided. The three-way valve 23 is connected to the calculating means 28 as described later, and the calculating means 28 is
By controlling the three-way valve 23, the cooling water is passed through the heat exchanger 21 when the liquid temperature of the electrodeposition coating material 3 is lowered, and the cooling water is passed through the bypass flow passage 22 when the liquid temperature of the electrodeposition coating material 3 is not lowered to control the temperature. To do.
【0017】電着槽2の電着塗料3中には電極24が浸
漬されており、電極24と図示しない被塗物4用電極と
は電流検出手段である電流を時間に対して積算計量する
積算電流計25および電圧検出手段である電圧計26を
有する電源である交流電源27に整流器を含む電源回路
30および電源調整回路31を介して接続されている。The electrode 24 is immersed in the electrodeposition paint 3 in the electrodeposition tank 2, and the electrode 24 and the electrode for the object 4 to be coated (not shown) measure the current as a current detecting means by integrating with time. It is connected to an AC power supply 27 which is a power supply having an integrating ammeter 25 and a voltmeter 26 which is a voltage detecting means, via a power supply circuit 30 including a rectifier and a power supply adjusting circuit 31.
【0018】交流電源27から供給される交流電力は電
源回路30で整流化および平滑化された後、電源調整回
路31で予め定める電流および電圧に調整され、電極2
4が陽極となるように、電極24と被塗物4に接触して
いる図示しない電極との間に電圧が印加される。The AC power supplied from the AC power supply 27 is rectified and smoothed by the power supply circuit 30, and then adjusted to a predetermined current and voltage by the power supply adjusting circuit 31, and the electrode 2
A voltage is applied between the electrode 24 and an electrode (not shown) that is in contact with the object to be coated 4 so that 4 becomes an anode.
【0019】電着槽2中の電着塗料3には、電着塗料3
の液温を測定する温度検出手段である温度計29が浸漬
されている。The electrodeposition paint 3 in the electrodeposition tank 2 includes the electrodeposition paint 3
A thermometer 29 which is a temperature detecting means for measuring the liquid temperature is immersed.
【0020】認識手段6、流量計11,15、三方弁2
3、積算電流計25、電圧計26および温度計29は演
算手段28に接続されている。Recognition means 6, flow meters 11, 15 and three-way valve 2
3, the integrating ammeter 25, the voltmeter 26, and the thermometer 29 are connected to the calculating means 28.
【0021】図3は、電着塗料の液温と塗膜固有抵抗お
よびつきまわり性との関係を示すグラフである。温度と
塗膜固有抵抗との関係は直線L1で示され、温度とつき
まわり性との関係は直線L2で示されている。このグラ
フには、温度を上昇させればつきまわり性は向上するけ
れども、塗膜固有抵抗は低下することが示されている。FIG. 3 is a graph showing the relationship between the liquid temperature of the electrodeposition paint and the coating film specific resistance and throwing power. The relationship between the temperature and the coating film resistivity is shown by the straight line L1, and the relationship between the temperature and the throwing power is shown by the straight line L2. This graph shows that increasing the temperature improves throwing power, but decreases the coating film resistivity.
【0022】電着塗装を行えば、電着塗料3の組成が変
化し、塗膜固有抵抗が変動する。a値の塗膜固有抵抗を
得る際に、塗膜固有抵抗が電着塗料組成変化によってb
値まで下がれば、電着塗料液温をb値に対応する温度B
値からA値に下降させることによって塗膜固有抵抗とし
てa値を有する塗膜を得ることができることがわかる。
また、塗膜固有抵抗がc値に変動した場合も、電着塗料
の液温をc値に対応する温度であるC値からA値まで上
昇させればよい。When the electrodeposition coating is carried out, the composition of the electrodeposition coating 3 changes, and the coating film resistivity changes. When the coating resistance of a value is obtained, the coating resistance is changed by changing the composition of the electrodeposition coating b
If it falls to the value, the temperature of the electrodeposition coating liquid is the temperature B corresponding to the value b.
It can be seen that by lowering the value to the A value, it is possible to obtain a coating film having an a value as the coating resistance.
Further, even when the coating film resistivity fluctuates to the c value, the liquid temperature of the electrodeposition coating material may be raised from the C value, which is the temperature corresponding to the c value, to the A value.
【0023】任意の塗膜固有抵抗を得るための制御液温
T1は、数1に示されるように、現在の温度Tに係数k
を乗算することによって求めることができる。The control liquid temperature T1 for obtaining an arbitrary coating film resistivity is a coefficient k to the current temperature T as shown in the equation 1.
It can be obtained by multiplying by.
【0024】[0024]
【数1】T1 = T × k
次に前述の係数kの求め方について説明する。図4は、
筒状の被塗物35に塗膜36,37を形成した際の断面
図である。被塗物35の外側に塗膜36が形成され、内
側に塗膜37が形成されている。塗膜37の厚さをdと
する。## EQU00001 ## T1 = T.times.k Next, a method for obtaining the coefficient k will be described. Figure 4
It is sectional drawing at the time of forming the coating films 36 and 37 on the cylindrical object 35 to be coated. A coating film 36 is formed on the outside of the article 35, and a coating film 37 is formed on the inside. The thickness of the coating film 37 is d.
【0025】予め定める塗膜固有抵抗とつきまわり性と
を有する電着塗料を用いて電着塗装した際の内側の塗膜
37の厚さをd1とする。前述とは異なる塗膜固有抵抗
を有する電着塗料を用いて電着塗装した際の内側の塗膜
37の厚さをd2とする。係数kは数2に示されるよう
に厚さd1を厚さd2で除算することによって求められ
る。The thickness of the inner coating film 37 when electrodeposition coating is performed using an electrodeposition coating material having a predetermined coating film specific resistance and throwing power is d1. The thickness of the inner coating film 37 when electrodeposition coating is performed using an electrodeposition coating material having a coating film resistivity different from that described above is d2. The coefficient k is obtained by dividing the thickness d1 by the thickness d2 as shown in Equation 2.
【0026】[0026]
【数2】 [Equation 2]
【0027】この係数kは、電着塗料3の組成が変動
し、厚さd2が得られるような塗膜固有抵抗を示すよう
になった際に、そのときの温度Tから数1を用いて制御
温度T1を求める際に用いられる。When the composition of the electrodeposition coating material 3 changes so that the coating film has a specific resistance such that the thickness d2 is obtained, the coefficient k can be calculated from the temperature T at that time by using Equation 1. It is used when determining the control temperature T1.
【0028】塗膜固有抵抗が低くなれば、厚さdは厚く
なるため、係数kは1未満となり、制御温度T1は温度
Tよりも低くなる。また、塗膜固有抵抗が高くなれば、
厚さdは薄くなるため、係数kは1より大きくなり、制
御液温T1は液温Tより高くなる。As the coating film resistivity decreases, the thickness d increases, so the coefficient k becomes less than 1, and the control temperature T1 becomes lower than the temperature T. Also, if the coating film resistivity increases,
Since the thickness d becomes thin, the coefficient k becomes larger than 1, and the control liquid temperature T1 becomes higher than the liquid temperature T.
【0029】係数kは、電着塗料3の組成の変化に応じ
て複数の係数kを求め、演算手段18に記憶されてい
る。同様に前述とは異なるつきまわり性を示す電着塗料
についても同様に係数kを求め、後述する表1のような
塗膜固有抵抗とつきまわり性とのパラメータに対応する
係数kを示す表が作成され、予め演算手段28に記憶さ
れる。As the coefficient k, a plurality of coefficients k are calculated according to the change in the composition of the electrodeposition coating material 3, and are stored in the calculating means 18. Similarly, the coefficient k is similarly obtained for the electrodeposition coating material showing throwing power different from the above, and a table showing the coefficient k corresponding to the parameters of the coating film specific resistance and throwing power as shown in Table 1 below is obtained. It is created and stored in advance in the calculating means 28.
【0030】図5は、本発明の一実施例を示すフローチ
ャートである。ステップs1では、認識手段6によって
コンベア5が電着槽2に搬入する被塗物4の種類および
数量が認識され、ステップs2では、ステップs1で認
識された被塗物4の種類および数量が認識手段6から演
算手段28に出力される。ステップs3では、電圧計2
6によって測定された電圧が、演算手段28に出力され
る。FIG. 5 is a flow chart showing an embodiment of the present invention. In step s1, the recognition unit 6 recognizes the type and quantity of the article 4 to be conveyed by the conveyor 5 into the electrodeposition tank 2. In step s2, the type and quantity of the article 4 recognized in step s1 are recognized. It is output from the means 6 to the calculating means 28. In step s3, the voltmeter 2
The voltage measured by 6 is output to the calculating means 28.
【0031】ステップs4では、予め定められ、演算手
段28に入力されている時間Wが経過したか否かが演算
手段28によって判断され、時間Wが経過している場合
にはステップs5に進み、時間Wが経過していない場合
にはステップs1に戻る。時間Wを作業時間に対応して
設定してもよく、また、被塗物4が認識手段6によって
認識されてから塗装を完了するまでの時間に基づいて設
定してもよい。At step s4, it is judged by the calculating means 28 whether or not the time W which is set in advance and inputted to the calculating means 28 has elapsed. When the time W has elapsed, the routine proceeds to step s5, If the time W has not elapsed, the process returns to step s1. The time W may be set corresponding to the working time, or may be set based on the time from when the object to be coated 4 is recognized by the recognition means 6 to when the coating is completed.
【0032】ステップs5では、積算電流計25によっ
て測定された積算電流Iが演算手段28に出力され、ス
テップs6では、演算手段28によって時間W経過中に
ステップs3で入力された電圧が積算され、さらに時間
Wで除算されて平均電圧Vが算出される。In step s5, the integrated current I measured by the integrating ammeter 25 is output to the calculating means 28, and in step s6, the voltage input in step s3 while the time W has elapsed is integrated by the calculating means 28, Further, it is divided by the time W to calculate the average voltage V.
【0033】ステップs7では演算手段28によって、
ステップs2で入力された被塗物4の各種類に対応する
塗装面積と、数量との積算値を合計することによって、
総被塗物面積Sが算出される。At step s7, the calculating means 28
By summing the integrated values of the coating area and the quantity corresponding to each type of the article 4 input in step s2,
The total coated object area S is calculated.
【0034】ステップs8では、演算手段28によって
積算電流Iと平均電圧Eと総被塗物面積Sとを用いて、
数3から塗膜固有抵抗が算出される。被塗物4の抵抗
は、塗膜の抵抗に対して非常に小さいので、塗膜固有抵
抗算出時には考慮しなくてよい。In step s8, the calculating means 28 uses the integrated current I, the average voltage E, and the total area S of the object to be coated,
The coating film specific resistance is calculated from Equation 3. Since the resistance of the article to be coated 4 is extremely smaller than the resistance of the coating film, it does not have to be taken into consideration when calculating the coating film specific resistance.
【0035】[0035]
【数3】 [Equation 3]
【0036】ステップs9では、予め演算手段28に入
力されている表1から、予め定められ同じく演算手段2
8に入力されているつきまわり性と、ステップs8で算
出された塗膜固有抵抗とを用いて係数kが求められる。In step s9, from the table 1 which has been input to the calculating means 28 in advance, a predetermined calculating means 2 is also used.
The throwing power inputted in 8 and the coating film specific resistance calculated in step s8 are used to obtain the coefficient k.
【0037】[0037]
【表1】 [Table 1]
【0038】ステップs10では、演算手段28によっ
て温度計29から演算手段28に出力されている液温T
と、ステップs9で求められた係数kとから数1を用い
て制御液温が算出される。In step s10, the liquid temperature T output from the thermometer 29 to the calculating means 28 by the calculating means 28.
Then, the control liquid temperature is calculated using the equation 1 from the coefficient k obtained in step s9.
【0039】[0039]
【数1】T1 = T × k
ステップs11では、制御液温となるように演算手段2
8によって三方弁23が制御され、電着槽2内の電着塗
料3の液温が制御される。## EQU1 ## T1 = T.times.k At step s11, the calculating means 2 is operated so that the control liquid temperature is obtained.
The three-way valve 23 is controlled by 8 to control the liquid temperature of the electrodeposition coating material 3 in the electrodeposition tank 2.
【0040】ステップs12では塗装が終了か否かが判
断され、終了しない場合にはステップs1に戻り、終了
する場合には塗装操作を終了する。In step s12, it is judged whether or not the coating is completed. If it is not completed, the process returns to step s1. If it is completed, the coating operation is completed.
【0041】以上のように本実施例によれば、電着塗装
中に自動的に塗膜固有抵抗を求めることができ、求めら
れた塗膜固有抵抗から予め定めるつきまわり性を得るた
めの制御液温が求められ、電着槽内の電着塗料の液温を
制御することができる。As described above, according to this embodiment, the coating film specific resistance can be automatically obtained during the electrodeposition coating, and the control for obtaining the predetermined throwing power from the obtained coating film specific resistance. The liquid temperature is required, and the liquid temperature of the electrodeposition paint in the electrodeposition tank can be controlled.
【0042】したがって、電着塗装中に電着塗装条件の
制御を自動的に行うことができ、塗装品質を向上するこ
とができる。Therefore, the control of the electrodeposition coating conditions can be automatically performed during the electrodeposition coating, and the coating quality can be improved.
【0043】本実施例においては電極24と図示しない
被塗物4用電極との間に、電圧を印加したけれども、電
着槽2を金属製にして、被塗物4用電極と電着槽2との
間に電圧を印加しても、同様の効果が得られる。Although a voltage was applied between the electrode 24 and the electrode for the article to be coated 4 (not shown) in the present embodiment, the electrodeposition vessel 2 is made of metal and the electrode for the article to be coated 4 and the electrodeposition vessel The same effect can be obtained by applying a voltage between the two.
【0044】[0044]
【発明の効果】本発明によれば、電流と電圧と塗装面積
とを検出し、電流と電圧と塗装面積との間に演算を施し
て塗膜固有抵抗を求める。塗膜固有抵抗と予め定めるつ
きまわり性とのパラメータに対応する液温を算出し、前
記液温に基づいてつきまわり性を制御することができ
る。According to the present invention, the current, voltage and coating area are detected, and calculation is performed between the current, voltage and coating area to obtain the coating film specific resistance. The liquid temperature corresponding to the parameters of the coating film specific resistance and the predetermined throwing power can be calculated, and the throwing power can be controlled based on the liquid temperature.
【0045】したがって、つきまわり性が予め定められ
た値となるように自動的に液温が制御され、塗装品質を
向上することができる。Therefore, the liquid temperature is automatically controlled so that the throwing power becomes a predetermined value, and the coating quality can be improved.
【図1】本発明の一実施例である電着塗装装置1を示す
図である。FIG. 1 is a diagram showing an electrodeposition coating apparatus 1 which is an embodiment of the present invention.
【図2】図1に示される熱交換手段17を示す図であ
る。FIG. 2 is a diagram showing a heat exchange means 17 shown in FIG.
【図3】電着塗料の液温と塗膜固有抵抗およびつきまわ
り性との関係を示すグラフである。FIG. 3 is a graph showing the relationship between the liquid temperature of the electrodeposition coating composition and the coating film specific resistance and throwing power.
【図4】筒状の被塗物35に塗膜36,37を形成した
際の断面図である。FIG. 4 is a cross-sectional view when coating films 36 and 37 are formed on a tubular article 35 to be coated.
【図5】本発明の一実施例を示すフローチャートの一例
である。FIG. 5 is an example of a flowchart showing an embodiment of the present invention.
1 電着塗装装置 2 電着槽 3 電着塗料 4 被塗物 5 コンベア 6 認識手段 17 熱交換手段 21 熱交換器 24 電極 25 積算電流計 26 電圧計 27 交流電源 28 演算手段 29 温度計 30 電源回路 31 電流調整回路 1 Electro-deposition coating device 2 electrodeposition tank 3 electrodeposition paint 4 coated objects 5 conveyors 6 recognition means 17 Heat exchange means 21 heat exchanger 24 electrodes 25 Integrated ammeter 26 Voltmeter 27 AC power supply 28 computing means 29 Thermometer 30 power circuit 31 Current adjustment circuit
───────────────────────────────────────────────────── フロントページの続き (72)発明者 倉波 信男 兵庫県尼崎市南塚口町6丁目10番73号 神 東塗料株式会社内 ─────────────────────────────────────────────────── ─── Continued front page (72) Inventor Nobuo Kurami 6-1073 God, Minamitsukaguchi-cho, Amagasaki-shi, Hyogo Inside the East Paint Co., Ltd.
Claims (3)
を搬送し、この被塗物と電着槽内に貯留されている電極
との間に直流電源を接続し、電着塗装を行う電着塗装方
法において、 前記電源の電流と電圧と、さらに被塗物の塗装面積とを
検出し、 前記電流と電圧と塗装面積との間に演算を施して塗膜固
有抵抗を求め、 前記塗膜固有抵抗と予め定めるつきまわり性とのパラメ
ータに対応する電着塗料の液温を算出し、 前記液温となるように塗料の温度を変化し、これによっ
てつきまわり性を制御することを特徴とする電着塗装方
法。1. An object to be coated is conveyed into an electrodeposition tank containing an electrodeposition coating material, and a DC power source is connected between the object to be coated and an electrode stored in the electrodeposition tank to obtain an electrodeposition. In the electrodeposition coating method of performing coating, the current and voltage of the power source, and the coating area of the object to be coated are detected, and the coating resistance is calculated by performing a calculation between the current and voltage and the coating area. Obtained, calculate the liquid temperature of the electrodeposition paint corresponding to the parameters of the coating film specific resistance and the predetermined throwing power, change the temperature of the paint so as to be the liquid temperature, thereby controlling throwing power. An electrodeposition coating method characterized by:
きまわり性とをパラメータとする予め定めた係数を求
め、 前記係数と電着槽内の電着塗料の温度とを演算して求め
ることを特徴とする請求項1記載の電着塗装方法。2. The electrodeposition coating liquid temperature is obtained by calculating a predetermined coefficient using the coating film resistivity and throwing power as parameters, and calculating the coefficient and the temperature of the electrodeposition coating material in the electrodeposition tank. The electrodeposition coating method according to claim 1, which is obtained by
生手段と、 電流検出手段と電圧検出手段と塗装面積信号発生手段と
の各出力に応答し、塗膜固有抵抗を演算する第1演算手
段と、 つきまわり性を表す信号を導出するつきまわり性信号導
出手段と、 電着槽内の電着塗料の温度を検出する温度検出手段と、 電着槽内の電着塗料の温度を上昇または下降する熱交換
器と、 第1演算手段とつきまわり性信号導出手段との各出力に
応答し、塗膜固有抵抗とつきまわり性と電着塗料の温度
とを演算して目標液温を求める第2演算手段と、 第2演算手段の出力に応答して電着槽内の電着塗料が前
記目標液温になるように、前記熱交換器を制御する制御
手段とを含むことを特徴とする電着塗装装置。3. An electrodeposition tank containing an electrodeposition coating material, a transfer means for transferring and immersing an object to be coated into the electrodeposition tank, an electrode provided in the electrodeposition tank, and an object to be coated and an electrode. A power supply for supplying electric power between the two, a current detection means for detecting the current of the power supply, a voltage detection means for detecting the voltage of the power supply, and a coating area signal generator for deriving a signal representing the coating area of the object to be coated. Means, a first calculating means for calculating a coating film specific resistance in response to each output of the current detecting means, the voltage detecting means and the coating area signal generating means, and a throwing power signal for deriving a signal showing throwing power. Derivation means, temperature detection means for detecting the temperature of the electrodeposition coating material in the electrodeposition tank, heat exchanger for raising or lowering the temperature of the electrodeposition coating material in the electrodeposition tank, first computing means and throwing power. Responsive to each output from the signal deriving means, the coating film resistivity, throwing power and electrodeposition A second calculation means for calculating the target liquid temperature by calculating the temperature of the material, and the heat exchange so that the electrodeposition coating material in the electrodeposition tank reaches the target liquid temperature in response to the output of the second calculation means. An electrodeposition coating apparatus comprising a control means for controlling the container.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16463091A JPH059796A (en) | 1991-07-04 | 1991-07-04 | Electrodeposition coating method and device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16463091A JPH059796A (en) | 1991-07-04 | 1991-07-04 | Electrodeposition coating method and device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH059796A true JPH059796A (en) | 1993-01-19 |
Family
ID=15796856
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16463091A Pending JPH059796A (en) | 1991-07-04 | 1991-07-04 | Electrodeposition coating method and device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH059796A (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6333598A (en) * | 1986-07-28 | 1988-02-13 | Nissan Motor Co Ltd | Coating method by electrodeposition |
| JPS63297597A (en) * | 1987-05-29 | 1988-12-05 | Nissan Motor Co Ltd | Electrodeposition coating method |
-
1991
- 1991-07-04 JP JP16463091A patent/JPH059796A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6333598A (en) * | 1986-07-28 | 1988-02-13 | Nissan Motor Co Ltd | Coating method by electrodeposition |
| JPS63297597A (en) * | 1987-05-29 | 1988-12-05 | Nissan Motor Co Ltd | Electrodeposition coating method |
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