JPH0247295A - Electrodeposition coating device - Google Patents

Electrodeposition coating device

Info

Publication number
JPH0247295A
JPH0247295A JP19650988A JP19650988A JPH0247295A JP H0247295 A JPH0247295 A JP H0247295A JP 19650988 A JP19650988 A JP 19650988A JP 19650988 A JP19650988 A JP 19650988A JP H0247295 A JPH0247295 A JP H0247295A
Authority
JP
Japan
Prior art keywords
filtrate
tank
paint
electrodeposition
auxiliary
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP19650988A
Other languages
Japanese (ja)
Other versions
JPH044400B2 (en
Inventor
Noboru Fukumoto
福本 昇
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.)
Daihatsu Motor Co Ltd
Original Assignee
Daihatsu Motor 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 Daihatsu Motor Co Ltd filed Critical Daihatsu Motor Co Ltd
Priority to JP19650988A priority Critical patent/JPH0247295A/en
Publication of JPH0247295A publication Critical patent/JPH0247295A/en
Publication of JPH044400B2 publication Critical patent/JPH044400B2/ja
Granted legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Coating Apparatus (AREA)

Abstract

PURPOSE:To facilitate the resumption of the operation of an ultrafilter and to improve the efficiency in the filtration and recovery of a paint by replacing an electrodeposition paint in the ultrafilter with its filtrate when the operation of the title electrodeposition coating device provided with the ultrafilter is stopped. CONSTITUTION:The electrodeposition paint from the overflow vessel B of an electrodeposition bath A is introduced into the ultrafilter C, and filtered. The concd. paint is returned to the overflow vessel B through a pipe 11. The filtrate freed of paint by the filtration is introduced into a tank 12a and an auxiliary tank 12b, and then sent to a washing device W by a pump P2 to wash off the paint deposited on the surface of an electrodeposition-coated article. The filtrate is collected in a recovery tank 22, and then returned to the overflow vessel B. When the operation of the filtrafilter C is stopped, the electrodeposition paint in the ultrafilter C is replaced by the filtrate in the auxiliary tank 12b. Since the filtrate is sufficiently stored in the tank 12a when the operation is resumed, the washing filtrate can be supplied to the washing device W, hence the operation is smoothly resumed, and the efficiency in the filtration of paint is improved.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は電着塗装装置に関する。さらに詳しくは、電着
浴槽中の電着塗料を限外濾過装置によってン濾過し、そ
の濾液で出槽した被処理物を洗浄して持出された電着塗
料を回収するように構成されている電着塗装装置に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an electrodeposition coating apparatus. More specifically, the electrodeposition paint in the electrodeposition bath is filtered by an ultrafiltration device, and the filtrate is used to wash the treated material taken out of the tank, and the electrodeposition paint taken out is recovered. This article relates to an electrodeposition coating device.

[従来の技術] 自動車の製造ラインなどにおいて採用されている前記塗
料回収システムを備えた従来の電着塗装装置を第3図に
よって説明する。
[Prior Art] A conventional electrodeposition coating apparatus equipped with the above-mentioned paint recovery system, which is employed in automobile manufacturing lines, will be explained with reference to FIG.

(A)は電着浴槽、(B)はそのオーバーフロー槽であ
る。オーバーフロー槽(B)中の電着塗料は供給ポンプ
(Pl)により限外濾過装置(C)に送られ、そこでン
濾過される。濃縮された電着塗料はオーバーフロー槽(
B)に戻される。濾液は濾液タンク(D)に送られ、そ
こから濾液ポンプ(P2)により洗浄装置(讐)に送ら
れる。洗浄装置(讐)においては濾液を出槽してきた被
処理物に噴射して過剰に付着している電着塗料を洗い落
す。集められ洗液はオーバーフロー槽(B)に戻される
(A) is an electrodeposition bath, and (B) is its overflow tank. The electrocoating paint in the overflow tank (B) is sent by a supply pump (Pl) to an ultrafiltration device (C), where it is filtered. Concentrated electrodeposited paint is stored in an overflow tank (
B). The filtrate is sent to a filtrate tank (D) and from there to a cleaning device (envelope) by a filtrate pump (P2). In the cleaning device, the filtrate is sprayed onto the workpiece that has come out of the tank to wash off excess electrodeposited paint. The collected washing liquid is returned to the overflow tank (B).

電着塗装装置の定常運転時には前記のごとくして電着塗
料の回収が行なわれる。
During regular operation of the electrodeposition coating apparatus, the electrodeposition paint is recovered as described above.

[発明が解決しようとする課題] 近年省エネルギーの観点から、製造ラインの稼動時間以
外は限外濾過装置の運転を停止して消費電力の節減を図
ることが行なわれるようになってきている。
[Problems to be Solved by the Invention] In recent years, from the viewpoint of energy conservation, it has become common practice to stop the operation of ultrafiltration devices except during production line operating hours to reduce power consumption.

限外濾過装置を停止させるばあい、限外ン濾過膜の保護
のため、装置内の電着塗料をン濾液で置換し、ン濾液で
限外濾過膜を洗浄したのち停止する必要がある。このた
めに濾液タンク(D)中のン濾液を配管■により限外濾
過装置(C)に供給して置換を行なっている。そうする
と濾液タンク(D)中の濾液が減少した状態で運転が停
止されることになる。
In order to protect the ultrafiltration membrane, when the ultrafiltration apparatus is to be stopped, it is necessary to replace the electrocoating paint in the apparatus with the filtrate, wash the ultrafiltration membrane with the filtrate, and then stop the ultrafiltration apparatus. For this purpose, the filtrate in the filtrate tank (D) is supplied to the ultrafiltration device (C) via piping (2) for replacement. In this case, the operation will be stopped with the amount of filtrate in the filtrate tank (D) reduced.

このような状態で製造ラインが再稼動されると、限外ン
濾過装置(C)の運転開始初期においては濾液タンク(
D)を満水にするために洗浄装置(w)へン濾液を供給
することができず、そのため限外ン濾液による塗料回収
システムの本来の目的である塗料回収の効率が低下する
という問題がある。
When the production line is restarted under such conditions, the filtrate tank (
It is not possible to supply filtrate to the cleaning device (w) to fill D) with water, and as a result, there is a problem that the efficiency of paint recovery, which is the original purpose of the ultrafiltrate-based paint recovery system, decreases. .

本発明は前記の点に鑑みて、限外濾過装置の停止後の再
運転初期においても定常運転時と同等の塗料回収効率か
えられる電着塗装装置を提供せんとするものである。
In view of the above-mentioned points, the present invention aims to provide an electrodeposition coating apparatus that can achieve the same paint recovery efficiency as during steady operation even in the early stages of restarting the ultrafiltration apparatus after it has been stopped.

[課題を解決するための手段] 本発明は、電着浴槽中の電着塗料を限外濾過装置に送り
、その濾液を濾液タンクを介して洗浄装置に送り、該ン
濾液で出槽した被処理物を洗浄し、洗液を電着浴槽に戻
すようにされており、前記限外濾過装置の運転を停止す
る際には前記濾液で限外ン濾過装置内の塗料を置換した
のち停止するようにされている電着塗装装置において、
前記濾液タンクに加えて補助濾液タンクを設置し、前記
限外r濾過装置からの濾液配管を2系統に分けて濾液を
ぞれ濾液タンクと補助濾液タンクとに供給するようにし
、かつ該補助濾液タンクをオーバーフロー管により濾液
タンクに接続するとともに補助濾液タンクの下部から濾
液を前記限外濾過装置に送るように構成し、電着塗装装
置の定常運転時には限外濾過装置からのン濾液を前記2
系統に分かれた濾液配管から2濾液タンクおよび補助濾
液タンクにそれぞれ供給すると共に満水状態の補助濾液
タンクから濾液を濾液タンクにオーバーフローさせ、限
外濾過装置停止時には補助濾液タンク中の濾液を限外ン
濾過装置に送り装置内の塗料を該濾液で置換するように
してなる電着塗装装置に関する。
[Means for Solving the Problems] The present invention provides for sending the electrodeposition paint in the electrodeposition bath to an ultrafiltration device, sending the filtrate to a cleaning device via a filtrate tank, and using the filtrate to remove the coating material from the tank. The processed material is washed and the washing liquid is returned to the electrodeposition bath, and when the operation of the ultrafiltration device is stopped, the paint in the ultrafiltration device is replaced with the filtrate, and then the operation is stopped. In the electrodeposition coating equipment,
An auxiliary filtrate tank is installed in addition to the filtrate tank, and the filtrate piping from the ultrafiltration device is divided into two systems to supply the filtrate to the filtrate tank and the auxiliary filtrate tank, respectively, and the auxiliary filtrate is The tank is connected to the filtrate tank by an overflow pipe, and the filtrate is sent to the ultrafiltration device from the lower part of the auxiliary filtrate tank, and during steady operation of the electrodeposition coating device, the filtrate from the ultrafiltration device is transferred to the ultrafiltration device.
The filtrate is supplied to the two filtrate tanks and the auxiliary filtrate tank from the separate filtrate piping, and the filtrate is allowed to overflow from the auxiliary filtrate tank that is full to the filtrate tank, and when the ultrafiltration device is stopped, the filtrate in the auxiliary filtrate tank is drained into the ultrafiltrate tank. The present invention relates to an electrodeposition coating apparatus in which the filtrate is used to replace paint in a feeding device in a filtration device.

[作 用コ 限外ン濾過装置の運転を停止する際にはン濾液タンク中
のと濾液ではなく補助濾液タンク中の濾液で限外i濾過
装置内の塗料を置換して停止するようにされているので
、再運転時の濾液タンクには定常運転時と同様に所定量
の7濾液が溜っている。そのため再運転の初期から所定
量のン濾液を洗浄装置に供給できる。限外濾過装置から
の濾液配管を2系統にわけて濾液をそれぞれ濾液タンク
および補助濾液タンクに供給し、補助濾液タンクが満水
後は濾液を濾液タンクにオーバーフローさせることによ
って運転の全期間を通じてFp液タンクへの濾液流入量
はほぼ一定になる。
[Function] When the operation of the ultrafiltration device is stopped, the paint in the ultrafiltration device is replaced with the filtrate in the auxiliary filtrate tank, not the filtrate in the filtrate tank, and then the operation is stopped. Therefore, a predetermined amount of 7 filtrate is stored in the filtrate tank at the time of restarting the operation, as in the case of steady operation. Therefore, a predetermined amount of filtrate can be supplied to the cleaning device from the beginning of restart. The filtrate piping from the ultrafiltration device is divided into two systems, and the filtrate is supplied to the filtrate tank and the auxiliary filtrate tank, respectively. After the auxiliary filtrate tank is full, the filtrate overflows into the filtrate tank, so that the Fp liquid is maintained throughout the entire operation period. The amount of filtrate flowing into the tank becomes approximately constant.

[実施例] つぎに本発明を図面に基づいて説明する。[Example] Next, the present invention will be explained based on the drawings.

第1図は本発明の電着塗装装置の一実施例を示す概略説
明図である。
FIG. 1 is a schematic explanatory diagram showing an embodiment of the electrodeposition coating apparatus of the present invention.

電着浴槽(A)のオーバーフロー槽(B)中の電着塗料
は供給ポンプ(PL)により配管(ト))を通して限外
濾過装置(C)に送られ、そこで濾過される。
The electrodeposition paint in the overflow tank (B) of the electrodeposition bath (A) is sent to the ultrafiltration device (C) by a supply pump (PL) through piping (G)), where it is filtered.

限外濾過装置(C)で濃縮された電着塗料は配管(It
)によりオーバーフロー槽(B)に戻される。
The electrocoating paint concentrated in the ultrafiltration device (C) is transferred to the pipe (It
) is returned to the overflow tank (B).

濾液配管0力は配管(t2a)および配管(12b)に
分岐しており、濾液は配管(12a)および配管(12
b)から濾液タンク(D)および補助濾液タンク(E)
にそれぞれ送られる。補助濾液タンク(E)が満水状態
のときは濾液はオーバーフロー管(131により濾液タ
ンク(D)にオーバーフローされる。
The filtrate piping 0 force is branched into piping (t2a) and piping (12b), and the filtrate is transmitted through piping (12a) and piping (12b).
b) to filtrate tank (D) and auxiliary filtrate tank (E)
are sent to each. When the auxiliary filtrate tank (E) is full, the filtrate overflows into the filtrate tank (D) through the overflow pipe (131).

濾液タンク(D)中の濾液は濾液ポンプ(F2)により
配管Q41を通して洗浄装置(W)に送られる。
The filtrate in the filtrate tank (D) is sent to the washing device (W) through the pipe Q41 by the filtrate pump (F2).

洗浄装置(W)は、洗浄ブースの、濾液を被処理物に噴
射するライザ(2v、塗料含有ン濾液を溜める回収タン
クの、回収タンクn中の濾液をライザ(21)に供給す
るポンプのからなり、このような洗浄装置が複数段設け
られている。
The cleaning device (W) includes a riser (2v) in the cleaning booth that sprays filtrate onto the object to be treated, and a pump that supplies the filtrate in the recovery tank n to the riser (21) in the recovery tank that collects the filtrate containing paint. A plurality of stages of such cleaning devices are provided.

濾液タンク(D)からの濾液は最後段の回収タンクのに
送られ、ライザQυより被処理物に噴射されて被処理物
に付着して持出された電着塗料を洗い落したのち回収タ
ンクのに溜められる。
The filtrate from the filtrate tank (D) is sent to the last stage recovery tank, where it is sprayed from the riser Qυ onto the object to be treated, and after washing off the electrodeposition paint that has adhered to the object and taken out, it is sent to the recovery tank. It can be stored in.

回収タンクn中の塗料含有濾液はオーバーフロー管Q4
により前段の回収タンクのに送られる。
The paint-containing filtrate in the recovery tank n is transferred to the overflow pipe Q4.
It is sent to the previous stage recovery tank.

このように順次各段で洗浄に使用され塗料濃度が高めら
れた濾液は最前段の回収タンク面からポンプ□□□によ
り配管■を通してオーバーフロー槽(B)に戻される。
The filtrate, which has been used for cleaning in each stage in this way and has had an increased paint concentration, is returned to the overflow tank (B) from the surface of the collection tank at the first stage through the pipe (■) by the pump (□□□).

製造ラインの稼動を停止するばあいには、限外ン濾過装
置(C)への塗料の供給を停止したのち、補助濾液タン
ク(E)中の濾液をポンプ(F3)により配管口を通し
て限外濾過装置(C)の塗料供給側に送り、限外濾過装
置の運転を継続することにより装置内の塗料をン濾液で
置換する。置換作業が終了したのち限外濾過装置(C)
の運転および濾液タンク(D)から洗浄装置(W)への
濾液の供給を停止して、製造ラインの稼動を停止する。
When the operation of the production line is to be stopped, after stopping the supply of paint to the ultrafiltration device (C), the filtrate in the auxiliary filtrate tank (E) is pumped into the ultrafilter through the piping port by the pump (F3). The paint is sent to the paint supply side of the filtration device (C) and the ultrafiltration device continues to operate, thereby replacing the paint in the device with the filtrate. After the replacement work is completed, remove the ultrafiltration device (C)
and the supply of filtrate from the filtrate tank (D) to the washing device (W), and the operation of the production line is stopped.

このとき濾液タンク(D)は満水状態にある。At this time, the filtrate tank (D) is full of water.

製造ラインの再稼動時には、濾液タンク(D)は満水状
態にあるから、直ちに濾液を洗浄装置(W)に供給する
ことができる。なお、限外濾過装置(C)の再運転開始
時には補助濾液タンク(E)はほぼ空の状態であるから
、補助濾液タンク(E)が満水になり濾液タンク(D)
にオーバーフローするまでは濾液タンク(D)への濾液
流入速度は定常運転時より小さくなる。しかし補助濾液
タンク(E)への濾液流入量(F2)はそれほど大きく
する必要はなく (通常はつぎの運転停止時までに満水
になればよい)、配管(12a)からの濾液タンク(D
)への濾液流入量(Fl)に対する割合はする割合は F2 / Ft −8/100〜10/100程度であ
ればよいから、濾液タンク(D)から洗浄装置(W)へ
の濾液供給流量が塗料の回収効率に影響を与えるほど低
下することはない。また通常は運転開始時から補助濾液
タンク(E)が満水になり濾液タンク(D)にオーバー
フローするようになるまでの時間は480〜B00分程
度に設定される。
When the production line is restarted, the filtrate tank (D) is full of water, so the filtrate can be immediately supplied to the washing device (W). Note that the auxiliary filtrate tank (E) is almost empty when the ultrafiltration device (C) starts operating again, so the auxiliary filtrate tank (E) becomes full and the filtrate tank (D)
Until overflow occurs, the rate of filtrate flowing into the filtrate tank (D) is lower than during steady operation. However, the amount of filtrate flowing into the auxiliary filtrate tank (E) (F2) does not need to be that large (normally, it is enough to fill the water by the next time the operation is stopped), and the filtrate inflow from the piping (12a) (D
) to the filtrate inflow rate (Fl) should be about F2/Ft -8/100 to 10/100, so the filtrate supply flow rate from the filtrate tank (D) to the washing device (W) is It does not decrease enough to affect the paint recovery efficiency. Further, normally, the time from the start of operation until the auxiliary filtrate tank (E) becomes full of water and overflows to the filtrate tank (D) is set to about 480 to B00 minutes.

第2図に本発明の装置におけるる濾液タンク(D)と補
助濾液タンク(E)中の濾液の増減状況(1)を従来例
のそれ(II)と対比して示す。第2図において、■〜
■はつぎの状態を意味する。
FIG. 2 shows the increase/decrease situation (1) of the filtrate in the filtrate tank (D) and the auxiliary filtrate tank (E) in the apparatus of the present invention in comparison with that in the conventional example (II). In Figure 2, ■~
■ means the following state.

■定常運転時 ■運転停止時 ■再運転開始直後 ■再運転開始後しばらく経過したのち (たとえば数分後) 第2図から明らかなように、従来例では限外r濾過装置
の再運転開始から濾液タンクが満水になるまで(■−■
−■)はン濾液を洗浄装置に供給することは不可能であ
るのに対して、本発明では限外濾過装置の運転開始初期
から停止時まで、すなわち限外濾過装置の運転時は常に
ン濾液を洗浄装置に所定量供給できる。
■ During steady operation ■ When operation is stopped ■ Immediately after restarting operation ■ After a while (for example, several minutes) after restarting operation As is clear from Fig. 2, in the conventional example, from the time when the ultra-filter starts restarting Until the filtrate tank is full (■-■
-■) It is impossible to supply the filtrate to the cleaning device, whereas in the present invention, the ultrafiltration device is constantly supplied from the beginning of operation to the time of stopping, that is, when the ultrafiltration device is in operation. A predetermined amount of filtrate can be supplied to the cleaning device.

前記実施例においては、限外濾過装置停止時の濾液置換
は置換用濾液を限外r濾過膜に関し塗料流入側(順方向
)に供給して行なっているが、限外濾過装置まわりの配
管の接続を変更することにより、置換用濾液を限外ン濾
過膜に関し濾液流出側(逆方向)から供給して置換する
ようにしてもよい。
In the above embodiment, filtrate replacement when the ultrafiltration device is stopped is performed by supplying the replacement filtrate to the paint inflow side (forward direction) with respect to the ultrafiltration membrane. By changing the connection, the replacement filtrate may be supplied from the filtrate outflow side (reverse direction) of the ultrafiltration membrane for replacement.

[発明の効果] 電着塗装装置において、その塗料回収システムにおける
限外濾過装置の運転停止後の再運転時にその初期から濾
液を洗浄装置に供給することができ、限外濾過装置運転
時は常に所定の塗料回収効率かえられる。そのため限外
濾過装置の運転の開始および停止と自動車の製造ライン
の稼動のそれとを合致させることができ省エネルギーが
図れる。
[Effect of the invention] In an electrodeposition coating apparatus, filtrate can be supplied to the cleaning device from the initial stage when the ultrafiltration device in the paint recovery system is restarted after the operation is stopped, and the ultrafiltration device is always in operation. The specified paint recovery efficiency can be changed. Therefore, the start and stop of the operation of the ultrafiltration device can be made to coincide with the operation of the automobile production line, and energy saving can be achieved.

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

第1図は本発明の電着塗装装置の一実施例を示す概略説
明図、第2図は本発明の装置における濾液タンク中のF
rJ液の増減状況と従来例のそれとを対比する説明図、
第3図は従来例の電着塗装装置を示す概略説明図である
。 (図面の主要符号) (A)二電着浴槽 (C):限外ン濾過装置 第1 園 E:補助濾液タンク 14.15:配 管 (D):濾液タンク (E)コ補助濾液タンク (W):洗浄装置 02)、(12a) 、(12b)、 (141,6:配管
FIG. 1 is a schematic explanatory diagram showing one embodiment of the electrodeposition coating apparatus of the present invention, and FIG.
An explanatory diagram comparing the increase/decrease situation of rJ liquid and that of a conventional example,
FIG. 3 is a schematic explanatory diagram showing a conventional electrodeposition coating apparatus. (Main symbols in the drawing) (A) Double electrodeposition bath (C): Ultrafiltration device No. 1 Garden E: Auxiliary filtrate tank 14.15: Piping (D): Filtrate tank (E) Auxiliary filtrate tank ( W): Cleaning device 02), (12a), (12b), (141, 6: Piping

Claims (1)

【特許請求の範囲】[Claims] 1 電着浴槽中の電着塗料を限外濾液装置に送り、その
濾液を濾液タンクを介して洗浄装置に送り、該濾液で出
槽した被処理物を洗浄し、洗液を電着浴槽に戻すように
されており、前記限外濾過装置の運転を停止する際には
前記濾液で限外濾過装置内の塗料を置換したのち停止す
るようにされている電着塗装装置において、前記濾液タ
ンクに加えて補助濾液タンクを設置し、前記限外濾過装
置からの濾液配管を2系統に分けて濾液をぞれ濾液タン
クと補助濾液タンクとに供給するようにし、かつ該補助
濾液タンクをオーバーフロー管により濾液タンクに接続
するとともに補助濾液タンクの下部から濾液を前記限外
濾過装置に送るように構成し、電着塗装装置の定常運転
時には限外濾過装置からの濾液を前記2系統に分かれた
濾液配管から濾液タンクおよび補助濾液タンクにそれぞ
れ供給すると共に満水状態の補助濾液タンクから濾液を
濾液タンクにオーバーフローさせ、限外濾過装置停止時
には補助濾液タンク中の濾液を限外濾過装置に送り装置
内の塗料を該濾液で置換するようにしてなる電着塗装装
置。
1. Send the electrodeposition paint in the electrodeposition bath to the ultrafiltrate device, send the filtrate to the cleaning device via the filtrate tank, wash the object to be treated taken out of the tank with the filtrate, and transfer the washing liquid to the electrodeposition bath. In the electrodeposition coating apparatus, the filtrate tank is configured to return to its original state, and when the operation of the ultrafiltration apparatus is stopped, the paint in the ultrafiltration apparatus is replaced with the filtrate before the operation is stopped. In addition, an auxiliary filtrate tank is installed, and the filtrate piping from the ultrafiltration device is divided into two systems to supply filtrate to the filtrate tank and the auxiliary filtrate tank, respectively, and the auxiliary filtrate tank is connected to an overflow pipe. is connected to the filtrate tank, and the filtrate is sent to the ultrafiltration device from the lower part of the auxiliary filtrate tank, and during steady operation of the electrodeposition coating device, the filtrate from the ultrafiltration device is divided into the two systems. The filtrate is supplied from the piping to the filtrate tank and the auxiliary filtrate tank, and the filtrate is allowed to overflow from the auxiliary filtrate tank that is full to the filtrate tank, and when the ultrafiltration device is stopped, the filtrate in the auxiliary filtrate tank is sent to the ultrafiltration device. An electrodeposition coating device that replaces paint with the filtrate.
JP19650988A 1988-08-05 1988-08-05 Electrodeposition coating device Granted JPH0247295A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19650988A JPH0247295A (en) 1988-08-05 1988-08-05 Electrodeposition coating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19650988A JPH0247295A (en) 1988-08-05 1988-08-05 Electrodeposition coating device

Publications (2)

Publication Number Publication Date
JPH0247295A true JPH0247295A (en) 1990-02-16
JPH044400B2 JPH044400B2 (en) 1992-01-28

Family

ID=16358935

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19650988A Granted JPH0247295A (en) 1988-08-05 1988-08-05 Electrodeposition coating device

Country Status (1)

Country Link
JP (1) JPH0247295A (en)

Also Published As

Publication number Publication date
JPH044400B2 (en) 1992-01-28

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