JPS5980796A - Electrodeposition painting device - Google Patents

Electrodeposition painting device

Info

Publication number
JPS5980796A
JPS5980796A JP19015582A JP19015582A JPS5980796A JP S5980796 A JPS5980796 A JP S5980796A JP 19015582 A JP19015582 A JP 19015582A JP 19015582 A JP19015582 A JP 19015582A JP S5980796 A JPS5980796 A JP S5980796A
Authority
JP
Japan
Prior art keywords
diaphragm
water
chamber
diaphragm chamber
electrodeposition
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
JP19015582A
Other languages
Japanese (ja)
Inventor
Makoto Nakayama
真 中山
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.)
Mazda Motor Corp
Original Assignee
Mazda Motor 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 Mazda Motor Corp filed Critical Mazda Motor Corp
Priority to JP19015582A priority Critical patent/JPS5980796A/en
Publication of JPS5980796A publication Critical patent/JPS5980796A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To form easily a paint coated film having different thickness at upper and lower side by providing plural diaphragm chambers which are divided to upper and lower chambers in an electrodeposition cell, transferring a part of the diaphragm water in the upper diaphragm chambers into the lower diaphragm chambers and making the conductivity of the diaphragm water smaller on the upper side than on the lower side. CONSTITUTION:Plural pairs of diaphragm chambers each consisting of an upper diaphragm chamber 7 and a lower diaphragm chamber 8 are juxtaposed on both sides in an electrodeposition cell 2, and diaphragms 7a, 8a and plates 9, 10 are provided in the upper and lower chambers 7, 8. The upper chamber 7 is connected through a supply pipe 12 to a regulation tank 13, and is further connected through a conduit 14 for circulation to the tank 13. The conductivity of the diaphragm water in the tank 13 is measured with a sensor 15 and pure water is supplied by a flow rate control valve 16 to the tank 13 to regulate the conductivity of the diaphragm water to about 50- 100muOMEGA/cm. Said diaphragm water is supplied by a pump 11 into the chamber 7. Part of the diaphragm water discharged from the chamber 7 is introduced through a three-way valve 18 provided to the conduit 14 into the chamber 8, and regulate the conductivity of the diaphragm water therein to 150-300muOMEGA/cm. The thickness of the paint coated film is thus made thin on the upper side and thick on the lower side.

Description

【発明の詳細な説明】 本発明は電着塗装装置、殊に電着槽内に設けた隔膜室に
電極を配置し該電極と被塗物との間に電圧を印加して塗
料を被塗物に付着させるようにした隔膜式電着塗装装置
に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides an electrodeposition coating apparatus, in particular, a method in which an electrode is arranged in a diaphragm chamber provided in an electrodeposition tank, and a voltage is applied between the electrode and the object to be coated to coat the object. This invention relates to a diaphragm-type electrodeposition coating device that is adapted to adhere to objects.

水分散性または水溶性の電着塗料を含む液を電着槽内に
満たし、該電着槽に電極を設けて該電極と電着槽内に浸
漬された被塗物との間に直流電圧を印加し、被塗物に塗
料を静電的に付着させるようになった電着塗装は、自動
車車体の塗装等に広く採用されている。ところで、自動
車車体は、下部が上部に比し腐蝕条件が苛酷であるため
、塗料膜は下部が上部よシ厚くなるようにする必要があ
る。従来、電着塗装においてこの目的を達成するために
、特開昭52−127946号には、電着槽の内壁面に
沿って絶縁性遮蔽板を設け、この遮蔽板と被塗物との間
に電着槽より弱い電圧を与えられる電極板を配置するこ
とによシ、被塗物表面のうちの遮蔽板に対応する部位に
は薄く、他の部位には厚い塗膜を形成できるようにした
装置が提案されている。また、特開昭52−12794
8号には、自動車車体の電着塗装において、まず車体下
部を高電圧電着槽に浸漬して塗装を行ない、次いで車体
全部を低電圧電着槽に浸漬することによシ、下部は厚く
、上部は薄い塗膜を形成する方法が提案されている。
An electrodeposition tank is filled with a liquid containing a water-dispersible or water-soluble electrodeposition paint, an electrode is provided in the tank, and a DC voltage is applied between the electrode and the object to be coated immersed in the tank. Electrodeposition coating, in which paint is applied electrostatically to the object to be coated, is widely used for painting automobile bodies and the like. Incidentally, since the lower part of an automobile body is subject to more severe corrosion conditions than the upper part, the paint film must be thicker at the lower part than at the upper part. Conventionally, in order to achieve this objective in electrodeposition coating, Japanese Patent Application Laid-open No. 127946/1987 discloses that an insulating shielding plate is provided along the inner wall surface of the electrodeposition tank, and the gap between this shielding plate and the object to be coated is By arranging an electrode plate that can apply a voltage weaker than that of the electrodeposition bath, it is possible to form a thin coating film on the part of the surface of the object to be coated that corresponds to the shielding plate, and a thick coating film on other parts. A device has been proposed. Also, JP-A-52-12794
No. 8 states that in electrodeposition painting of automobile bodies, the lower part of the car body is first immersed in a high-voltage electrodeposition bath, and then the entire body is immersed in a low-voltage electrodeposition bath, so that the lower part is thicker. , a method has been proposed in which a thin coating film is formed on the top.

このような従来の電着塗装においては、電着槽内の電着
液に電極が裸で挿入されるか、或いは電着槽自体が電極
を構成するものであシ、塗装の進行に伴なって電着液中
の塗料成分が被塗物に付着し、その分だけ中和剤の濃度
が高くなシ、塗膜の膜厚が薄くなる傾向を生ずる。この
問題を解決するため、電着槽内に浸透性隔膜によシ囲ま
れた隔膜室を設け、この隔膜室内に電極を配置すること
によシ、被塗物に付着した塗料の量に相当する量の中和
剤を該隔膜室に移し、電着液中の中和剤濃度を塗料濃度
に対し適正に制御するようにした隔膜式電着塗装が使用
されるようになって来ている。
In such conventional electrodeposition coating, the electrode is inserted bare into the electrodeposition liquid in the electrodeposition tank, or the electrodeposition tank itself constitutes the electrode, and as the coating progresses, the electrode is inserted into the electrodeposition solution. As a result, the paint components in the electrodeposition solution adhere to the object to be coated, and the concentration of the neutralizing agent becomes correspondingly high, resulting in a tendency for the thickness of the coating film to become thinner. In order to solve this problem, a diaphragm chamber surrounded by a permeable diaphragm is provided in the electrodeposition bath, and an electrode is placed inside this diaphragm chamber. A diaphragm-type electrodeposition coating in which an amount of neutralizing agent is transferred to the diaphragm chamber, and the concentration of the neutralizing agent in the electrodeposition solution is appropriately controlled relative to the concentration of the paint, has come into use. .

しかし、上述した特開昭52−127946号によシ提
案された装置は、このような隔膜式電着塗装に適したも
のとは言えず、十分に満足な結果は期待できなめ。また
、特開昭52−127948号によシ提案された方法は
、厚さの異なる塗膜を形成するために二工程を必要とし
、設備の面からも処理時間の面からも満足できるもので
はない。
However, the apparatus proposed in JP-A-52-127946 mentioned above cannot be said to be suitable for such diaphragm-type electrodeposition coating, and cannot be expected to produce fully satisfactory results. Furthermore, the method proposed in JP-A-52-127948 requires two steps to form coating films of different thicknesses, and is not satisfactory in terms of equipment and processing time. do not have.

本発明は、従来の電着塗装の上述した問題に着目して得
られたもので、簡単な装置により上下で厚さの異る塗膜
を形成することができる隔膜式電着塗装装置を提供する
ことを目的とする。
The present invention was achieved by focusing on the above-mentioned problems of conventional electrodeposition coating, and provides a diaphragm-type electrodeposition coating device that can form coating films with different thicknesses on the upper and lower sides using a simple device. The purpose is to

すなわち、本発明は、電着槽内の隔膜室内に電極が配置
され、電着槽内に浸漬された被塗物と電極との間に直流
電圧を印加することにより被塗物表面に塗料を電着させ
、被塗物の塗装を行なうようになった電着塗装装置にお
いて、隔膜室は上下に分割され、各々の隔膜室に電極が
配置されるとともに、上側の隔膜室の隔膜水を下側の隔
膜室に移すことによシ上側の隔膜室の隔膜水の電導塵を
下側の隔膜室の隔膜水の電導塵よシ小さくするようにし
たことを特徴とする。本発明のこの構成によれば、下側
の隔膜室の隔膜水の電導塵が上側の隔膜室よシ大きいの
で、被塗物下部の電流密度が上部より高くなシ、下部に
形成される塗膜は上部よシ厚くなる。上側の隔膜室から
下側の隔膜室に隔膜水を移すには、隔膜水を上側隔膜室
から取シ出して中和剤濃度調整の上、再びこの隔膜室に
戻す循環径路中に三方弁を設け、一方の出口を下側隔膜
室に接続するようにしてもよく、この場合には下側隔膜
室の隔膜水の電導塵の調整が容易であるとともに、調整
槽の隔膜水の電導塵の調整も容易となる。電導塵は上側
の隔膜室に供給される時点で50〜100μヒ/儒程度
に調整槽によって調整し、下側の隔膜室には隔膜水雷導
度が150〜600μ’117cm程度になるように上
側の隔膜室から隔膜水を循環させることが好ましい。上
側の隔膜室の隔膜水の電導塵が50μυ/cr11以下
の場合には形成される塗膜が薄くなシすぎ、100μT
J/cm以上では厚くなシすぎて不経済である。下側の
隔膜室の隔膜水の電導塵は、普通の自動車車体下部に要
求される塗膜厚さを確保するために150〜300μσ
/−とした。
That is, in the present invention, an electrode is arranged in a diaphragm chamber in an electrodeposition tank, and a DC voltage is applied between the electrode and a workpiece immersed in the electrodeposition tank, thereby applying paint to the surface of the workpiece. In electrocoating equipment that uses electrodeposition to paint objects, the diaphragm chamber is divided into upper and lower halves, and an electrode is placed in each diaphragm chamber, and the diaphragm water in the upper diaphragm chamber is drained. By moving the diaphragm to the side diaphragm, the conductive dust in the diaphragm water in the upper diaphragm is made smaller than that in the diaphragm water in the lower diaphragm. According to this configuration of the present invention, since the electrically conductive dust in the diaphragm water in the lower diaphragm chamber is larger than that in the upper diaphragm chamber, the current density in the lower part of the object to be coated is higher than in the upper part. The membrane becomes thicker at the top. To transfer diaphragm water from the upper diaphragm chamber to the lower diaphragm chamber, a three-way valve is installed in the circulation path that takes the diaphragm water from the upper diaphragm chamber, adjusts the neutralizing agent concentration, and returns it to this diaphragm chamber. In this case, it is easy to adjust the conductive dust in the diaphragm water in the lower diaphragm chamber, and to control the conductive dust in the diaphragm water in the adjustment tank. Adjustment is also easy. When the conductive dust is supplied to the upper diaphragm chamber, it is adjusted to about 50 to 100 μm/f in a regulating tank, and the upper diaphragm is adjusted to a diaphragm torpedo conductivity of about 150 to 600 μ'117 cm in the lower diaphragm chamber. Preferably, the diaphragm water is circulated from the diaphragm chamber. If the conductive dust in the diaphragm water in the upper diaphragm chamber is less than 50μυ/cr11, the coating film formed will be too thin and will be 100μT.
J/cm or more is too thick and uneconomical. The conductive dust of the diaphragm water in the lower diaphragm chamber is 150 to 300 μσ to ensure the coating thickness required for the lower part of a normal automobile body.
/-.

以下、本発明の実施例を図について説明する。Embodiments of the present invention will be described below with reference to the drawings.

第1図において、塗料と中和剤を含む電着溶液1が満た
された電着槽2は、被塗物人口3及び出口4を有し、被
塗物5はコンベヤ6により入口3から電着槽2内を通電
、出口4から搬出される。電着槽2内には、上側隔膜室
7と下側隔膜室8を対とした複数対の隔膜室が、被塗物
の進行方向に沿って両側に列状に配置されている。第2
図に示すように、上側隔膜室7は被塗物5側の壁面に浸
透性隔膜7aを有し、内部には上側極板9が配置されて
いる。同様に、下側隔膜室8は隔膜8aを有し、内部に
は下側極板10が配置されている。本発明がアニオン型
電着塗装に適用される場合には、極板9.10は電源の
負側に、被塗物5は正側にそれぞれ接続される。カチオ
ン型電着塗装の場合には、電源への接続はその逆になる
。周知のように、隔膜7 a s 8 aは車体に付着
した塗料の量に相当する量の中和剤をイオン交換作用に
よシ隔膜室7.8内に透過させ、電着槽2内の溶液の中
和剤濃度を塗料に対し適正に保つ。
In FIG. 1, an electrodeposition tank 2 filled with an electrodeposition solution 1 containing a paint and a neutralizing agent has an object to be coated 3 and an outlet 4, and an object to be coated 5 is supplied to the electrode from the inlet 3 by a conveyor 6. The inside of the loading tank 2 is energized, and it is carried out from the outlet 4. In the electrodeposition tank 2, a plurality of pairs of diaphragm chambers, each pair being an upper diaphragm chamber 7 and a lower diaphragm chamber 8, are arranged in rows on both sides along the traveling direction of the object to be coated. Second
As shown in the figure, the upper diaphragm chamber 7 has a permeable diaphragm 7a on the wall surface on the side of the object to be coated 5, and an upper electrode plate 9 is arranged inside. Similarly, the lower diaphragm chamber 8 has a diaphragm 8a, and a lower electrode plate 10 is disposed therein. When the present invention is applied to anionic electrodeposition coating, the electrode plates 9 and 10 are connected to the negative side of the power source, and the object to be coated 5 is connected to the positive side. In the case of cationic electrocoating, the connection to the power source is the opposite. As is well known, the diaphragm 7a s 8a allows an amount of neutralizing agent corresponding to the amount of paint adhering to the car body to permeate into the diaphragm chamber 7.8 by ion exchange, and the amount of neutralizing agent in the electrodeposition tank 2 is increased. Keep the neutralizer concentration in the solution appropriate for the paint.

再び第1図を参照すると、上側隔膜室7はポンプ11を
有する供給管12により調整槽13に接続され、該調整
槽13において電導塵が調整された隔膜水が供給管12
を介して上側隔膜室7に供給される。上側隔膜室7はさ
らに隔膜水循環用導管14によシ調整槽13に接続され
、上側隔膜室7において中和剤濃度が高まシその結果と
して電導塵が高くなった隔膜水は調整槽13に排出され
る。調整槽13には、電導塵センサ15からの信号によ
り開度を調整される流量制御弁16を有する給水管17
が設けられ、該給水管17から調整槽13に純水が供給
されて該調整槽13内の隔膜水の電導塵を所定の値、た
とえば50〜1[]0μぴ々に調整する。
Referring again to FIG. 1, the upper diaphragm chamber 7 is connected to a regulating tank 13 by a supply pipe 12 having a pump 11, and the diaphragm water in which conductive dust has been adjusted in the regulating tank 13 is supplied to the supply pipe 12.
It is supplied to the upper diaphragm chamber 7 via. The upper diaphragm chamber 7 is further connected to the adjustment tank 13 by a diaphragm water circulation conduit 14, and the diaphragm water in which the neutralizing agent concentration is high in the upper diaphragm chamber 7 and the conductive dust is high as a result is transferred to the adjustment tank 13. be discharged. The adjustment tank 13 includes a water supply pipe 17 having a flow rate control valve 16 whose opening degree is adjusted by a signal from the conductive dust sensor 15.
is provided, and pure water is supplied from the water supply pipe 17 to the adjustment tank 13 to adjust the conductive dust in the diaphragm water in the adjustment tank 13 to a predetermined value, for example, exactly 50 to 1[]0μ.

導管14には三方弁18が設けられ、該導管14はこの
三方弁18を介して下側隔膜室8に接続されている。三
方弁18は上側隔膜室7から排出された隔膜水を所定量
だけ下側隔膜室8に導入するように働らく。下側隔膜室
8には隔膜水排出管19が設けられている。上側隔膜室
7から下側隔膜室8へ導かれる隔膜水の量は、下側隔膜
室8の隔膜水の電導塵が所定の範囲たとえば150〜3
00μU/αになるように調整し、その調整は三方弁1
8によって行なう。
The conduit 14 is provided with a three-way valve 18 via which it is connected to the lower diaphragm chamber 8 . The three-way valve 18 functions to introduce a predetermined amount of diaphragm water discharged from the upper diaphragm chamber 7 into the lower diaphragm chamber 8 . A diaphragm water discharge pipe 19 is provided in the lower diaphragm chamber 8 . The amount of diaphragm water guided from the upper diaphragm chamber 7 to the lower diaphragm chamber 8 is such that the conductive dust of the diaphragm water in the lower diaphragm chamber 8 is within a predetermined range, for example, 150 to 3
Adjust so that it is 00μU/α, and use the three-way valve 1 to adjust it.
Do it by 8.

このように、隔膜水の電導塵は下側隔膜室8の方が上側
隔膜室7よシ高いので、隔膜電流も下側隔膜室8の方が
高くなシ、その結果、被塗物に形成される塗膜は下部が
厚くなる。尚、図示実施例では、上側隔膜室から調整槽
に至る隔膜水循環回路から隔膜水の一部を下側隔膜室に
移すよ・うに構成しているが、上側隔膜室から取り出さ
れる隔膜水の全量を下側隔膜室に導びき、下側隔膜室か
ら取シ出される隔膜水を調整槽に移すか或いは廃棄する
ようにしてもよい。
In this way, since the conductive dust in the diaphragm water is higher in the lower diaphragm chamber 8 than in the upper diaphragm chamber 7, the diaphragm current is also higher in the lower diaphragm chamber 8, and as a result, it forms on the object to be coated. The coating film is thicker at the bottom. In the illustrated embodiment, a portion of the diaphragm water is transferred from the diaphragm water circulation circuit extending from the upper diaphragm chamber to the adjustment tank to the lower diaphragm chamber, but the total amount of diaphragm water taken out from the upper diaphragm chamber The diaphragm water may be introduced into the lower diaphragm chamber, and the diaphragm water taken out from the lower diaphragm chamber may be transferred to an adjustment tank or discarded.

以上説明した構造の電着塗装装置を用いて、次の電着条
件によシミ着塗装を行なった。
Using the electrodeposition coating apparatus having the structure described above, stain coating was carried out under the following electrodeposition conditions.

電着槽:長さ350、幅2.5m%深さ2m隔膜室:高
さ上側0.8m、下側1−2m5幅1m、厚さ0.1m
、個数(片側配 置)各14個 被塗物:自動車の車体 総表面積60m2塗 料:0T
O−U−52(日本ペイント社製) 電導塵  1400 tiTJ/cm 温  度   27℃ 濃  度   21% クーロン効率33■/C 印加電圧:330V(カチオン・型) 被塗物の電着槽への全没時間2.5分 被塗′物の電着槽への全没数 4個 以上の電着条件で上側隔膜室7および下側隔膜室8の隔
膜水の電導塵を変えた場合の被塗物5と上側極板9およ
び下側極板lOとの間に流れる電着槽2内の総隔膜電流
は第3図に示すように変化し、この総隔膜電流の変化に
対する塗膜の厚さは第4図に示すように変化する。
Electrodeposition bath: length 350, width 2.5m% depth 2m Diaphragm chamber: height 0.8m on top, 1-2m on bottom 5m width 1m, thickness 0.1m
, Number of pieces (placed on one side) 14 each Object to be coated: Automobile body Total surface area 60m2 Paint: 0T
O-U-52 (manufactured by Nippon Paint Co., Ltd.) Conductive dust 1400 tiTJ/cm Temperature 27°C Concentration 21% Coulombic efficiency 33■/C Applied voltage: 330V (cation/type) Total charge of the object to be coated to the electrodeposition bath Immersion time: 2.5 minutes Total number of objects to be coated immersed in the electrodeposition tank Coatings when the conductive dust in the diaphragm water in the upper diaphragm chamber 7 and lower diaphragm chamber 8 is changed under the conditions of electrodeposition of 4 or more objects The total diaphragm current in the electrodeposition tank 2 flowing between the object 5 and the upper electrode plate 9 and the lower electrode plate lO changes as shown in FIG. changes as shown in FIG.

上記の電着条件で上側隔膜室7の隔膜水の電導塵を10
0μU/−、下側隔膜室8の隔膜水の電導塵を200μ
U/Crnとした場合の塗膜の厚さは、被塗物の上部で
は約15μ、下部では約18μの塗膜厚さが得られた。
Under the above electrodeposition conditions, the conductive dust in the diaphragm water in the upper diaphragm chamber 7 was
0μU/-, 200μ of conductive dust in the diaphragm water in the lower diaphragm chamber 8
As for the coating thickness in the case of U/Crn, a coating thickness of about 15μ was obtained on the upper part of the object to be coated, and about 18μ on the lower part.

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

第1図は本発明の一実施例を示す電着塗装装置の側面図
、第2図はその一部断面図、第3図は上側および下側隔
膜室の隔膜水の電導塵を変えた場合の被塗物と上側およ
び下側極板との間に流れる総隔膜電流の変化を示すグラ
フ、第4図は総隔膜電流に対する塗膜厚さの変化を示す
グラフである。 2・・・電着槽、5・・・被塗物、7・・・上側隔膜室
、8・・・下側隔膜室、9,10・・・電極板、17・
・・給水管、18・・・三方弁。 特許出願人  東洋工業株式会社
Fig. 1 is a side view of an electrodeposition coating apparatus showing an embodiment of the present invention, Fig. 2 is a partial sectional view thereof, and Fig. 3 is a case where the conductive dust in the diaphragm water in the upper and lower diaphragm chambers is changed. FIG. 4 is a graph showing changes in the total diaphragm current flowing between the object to be coated and the upper and lower electrode plates, and FIG. 4 is a graph showing changes in coating film thickness with respect to the total diaphragm current. 2... Electrodeposition tank, 5... To be coated, 7... Upper diaphragm chamber, 8... Lower diaphragm chamber, 9, 10... Electrode plate, 17.
... Water supply pipe, 18... Three-way valve. Patent applicant: Toyo Kogyo Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 電着塗料液が充満された電着槽内に隔膜室が設けられ該
隔膜室内に電極板が配置され、この電極板と、前記電着
槽内に浸漬された被塗物との間に直流電圧を印加して被
塗物の表面に塗料を電着させることにより被塗物の塗装
を行なうようになった電着塗装装置において、前記隔膜
室は上下に分割されて各々の隔膜室に電極板が配置され
、上側の隔膜室の隔膜水の少くとも一部を下側の隔膜室
に移す回路が設けられ、上側の隔膜室の隔膜水の電導塵
が下側の隔膜室の隔膜水の電導塵より小さくなるように
構成されたことを特徴とする電着塗装装置、
A diaphragm chamber is provided in an electrodeposition tank filled with an electrodeposition paint solution, an electrode plate is arranged in the diaphragm chamber, and a direct current is applied between the electrode plate and the object to be coated immersed in the electrodeposition tank. In an electrodeposition coating apparatus that coats an object by electrodepositing the paint onto the surface of the object by applying a voltage, the diaphragm chamber is divided into upper and lower parts, and each diaphragm chamber is provided with an electrode. A plate is arranged, and a circuit is provided to transfer at least a portion of the diaphragm water in the upper diaphragm chamber to the lower diaphragm chamber, such that conductive dust in the diaphragm water in the upper diaphragm chamber is transferred to the diaphragm water in the lower diaphragm chamber. An electrodeposition coating device configured to be smaller than conductive dust,
JP19015582A 1982-10-29 1982-10-29 Electrodeposition painting device Pending JPS5980796A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19015582A JPS5980796A (en) 1982-10-29 1982-10-29 Electrodeposition painting device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19015582A JPS5980796A (en) 1982-10-29 1982-10-29 Electrodeposition painting device

Publications (1)

Publication Number Publication Date
JPS5980796A true JPS5980796A (en) 1984-05-10

Family

ID=16253331

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19015582A Pending JPS5980796A (en) 1982-10-29 1982-10-29 Electrodeposition painting device

Country Status (1)

Country Link
JP (1) JPS5980796A (en)

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