JPS5891199A - Electrodeposition painting device - Google Patents
Electrodeposition painting deviceInfo
- Publication number
- JPS5891199A JPS5891199A JP19009581A JP19009581A JPS5891199A JP S5891199 A JPS5891199 A JP S5891199A JP 19009581 A JP19009581 A JP 19009581A JP 19009581 A JP19009581 A JP 19009581A JP S5891199 A JPS5891199 A JP S5891199A
- Authority
- JP
- Japan
- Prior art keywords
- cathode
- tank
- electrodeposition
- coating liquid
- storage tank
- 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
Links
Abstract
Description
【発明の詳細な説明】
本発明は、電着塗装装置に関L1 より詳しく述べると
連続的な電着塗装によっても電着塗装浴槽内の塗料の組
成変化を極微少に保持するこピができ、品質が一定した
塗装製品を常番壬安定して製造できる電着塗装装置に関
する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an electrodeposition coating device.More specifically, it is possible to maintain extremely slight changes in the composition of the paint in the electrodeposition coating bath even through continuous electrodeposition coating. The present invention relates to an electrodeposition coating device that can consistently and consistently produce coated products of consistent quality.
従来、金属物品を連続的に電着塗装すると電着塗装浴槽
中の塗料の組成が変化するため、品質が一定した塗装製
品かえられず、この欠点を解消するため種々の装置が提
案されている。 たとえば、電着塗装浴槽g=イオン交
換処理装装置限外!簿装置を##[て、雷着塗料をそれ
ぞれ単独で又は組合せて処理する装置が公知である。Conventionally, when metal articles are continuously electrocoated, the composition of the paint in the electrocoating bath changes, making it impossible to obtain a coated product of constant quality. Various apparatuses have been proposed to overcome this drawback. For example, electrodeposition coating bath g = ion exchange treatment equipment limit! Apparatuses for treating lightning coating paints either singly or in combination are known.
しかしながら、これらの装置を使用しても電着塗料の組
成変化を効率よく抑制し、その変化を極微少に保持し、
優れた塗装製品を安定して製造することはできなかった
。However, even when these devices are used, changes in the composition of the electrodeposition paint can be effectively suppressed, and the changes can be kept to a very small level.
It has not been possible to consistently produce superior painted products.
本発明は、前記従来の電着塗装装置では非常に困難な電
着塗料の組成変化を極微少に保持でき、一定の品質の電
着塗装製品を安定して供給できる電着塗装装置を提供す
ることを目的とするものである。The present invention provides an electrocoating device that can maintain extremely small changes in the composition of electrocoated paint, which is extremely difficult with the conventional electrocoating devices, and can stably supply electrocoated products of constant quality. The purpose is to
本発明の電着塗装装置を図面に基づき説明すると、電着
塗装浴槽/内は、マスキング材3により陽極帯域≠と陰
極帯域jとに区分されている。The electrodeposition coating apparatus of the present invention will be explained based on the drawings. The interior of the electrodeposition coating bathtub is divided by a masking material 3 into an anode zone ≠ and a cathode zone j.
本発明者の実験によれば、連続的な電着塗装を続けると
陰極帯域!の電着塗料のpHは陽極帯域弘のそれよりも
大巾に高くなることが明らかになつ6た。According to the inventor's experiments, if continuous electrodeposition coating is continued, the cathode zone! It was revealed that the pH of the electrodeposited paint was much higher than that of the anode band 6.
この高pHの電着塗料(以下、陰極塗装液と称す)を陰
極帯域≠内の任意の位置から任意の方法で電着塗装浴槽
外に取出し、導管を通じ陰極塗装液貯槽6に貯液する。This high-pH electrodeposition paint (hereinafter referred to as cathode coating liquid) is taken out of the electrodeposition coating bath from any position within the cathode zone≠ by any method, and stored in the cathode coating liquid storage tank 6 through a conduit.
ついで腋貯液は、イオン交換処理装置7に導管を通じ移
送し1イオン交換処理を施り低pH雷撃塗料とした後、
予備槽り又は(及び)電着塗装浴槽の陽極帯域jに導管
を通じて移送する。Next, the axillary liquid is transferred to the ion exchange treatment device 7 through a conduit and subjected to 1 ion exchange treatment to form a low pH lightning paint.
It is transferred through a conduit to the anode zone j of the pre-tank or/and electrocoating bath.
前記陰極塗装液は貯槽6に貯液することなく直接イオン
交換処理装置7に導管を通じ移送することもできる。The cathode coating liquid can also be directly transferred to the ion exchange treatment device 7 through a conduit without being stored in the storage tank 6.
前記イオン交換処理装置7は、カチオン交換樹脂を用賢
・て陰極塗装液中のカチオンを除去し低PH通過液とす
ることを主目的とす−るが、アニオン交換樹脂と併用(
混合又は組合せ)することができる。The main purpose of the ion exchange treatment device 7 is to use a cation exchange resin to remove cations from the cathode coating liquid and make it a low pH passing liquid, but it can also be used in combination with an anion exchange resin (
mixture or combination).
本発明の電着塗装装置は、以上のような処理系路を設け
たことを特徴とするが、さらに限外濾過装置りと組合せ
ることも好ましい。 限外濾過装置りは、陰極塗装液を
イオン交換処理を施す前の糸路に設電すればよ−・。
陰極塗装液を限外濾過処理すると、濃厚液と透過液0二
分離され濃厚液は陰極塗装液中1114又は(及び)電
着塗装浴槽の陽極帯斌弘に戻L1透過液はイオン交抄処
理7に移送できるよう導管を設ければよい。・この限外
#過処理によって陰極塗装液中のカチオン、アニオンは
、透過液中に含まれるため、これをイオン交換処理する
と、限外濾過を行わない場合と同様の効果がえられる。The electrodeposition coating apparatus of the present invention is characterized by being provided with the treatment system path as described above, but it is also preferable to further combine it with an ultrafiltration apparatus. For the ultrafiltration device, just install electricity in the thread path before the cathode coating liquid is subjected to ion exchange treatment.
When the cathode coating liquid is subjected to ultrafiltration treatment, the concentrated liquid and the permeated liquid are separated into two parts, and the concentrated liquid is returned to the cathode coating liquid (1114) or (and) the anode band of the electrodeposition coating bath and the L1 permeated liquid is subjected to ion exchange treatment. A conduit may be provided so that it can be transferred to 7. - As a result of this ultrafiltration treatment, the cations and anions in the cathode coating liquid are contained in the permeate, so if this is subjected to ion exchange treatment, the same effect as when no ultrafiltration is performed can be obtained.
又、該透過液は、塗料中の樹脂固形分をほとんど除去し
たものであるので、イオン交換処理の際に目づまりを起
すことが非常に少なり−と11う利点がある。Furthermore, since the permeate has almost all of the resin solid content in the paint removed, it has the advantage of being extremely unlikely to cause clogging during ion exchange treatment.
なお、上記説明における移送手段はポンプ(図示せず)
の使用が適当である。Note that the transfer means in the above explanation is a pump (not shown).
It is appropriate to use
以上説明したように本発明の電着塗装装置は、前記の糸
路を設けたことを特徴とし高pHの陰極帯域の電着塗料
をイオン交換処理するため、非常に効率よ(イオン交換
がなされ、又、イオン交換処理を施して得られる低pH
の通過液を予備槽jに貯液して、又はせずして電着塗装
浴槽の陽極帯域≠に戻すため、連続的な電着塗装によっ
て変化する電着塗装浴の組成を効率よく抑制でき、その
変化を極微少に保持でき、この結果、品質の一定な塗装
製品を安定して製造できると−1つ、優れた効果かえら
れる。As explained above, the electrodeposition coating apparatus of the present invention is characterized by being provided with the above-mentioned thread path, and performs ion exchange treatment on the electrodeposition paint in the high pH cathode zone. , and low pH obtained by ion exchange treatment.
Since the liquid passing through is returned to the anode zone of the electrocoating bath with or without storing it in the reserve tank j, it is possible to efficiently suppress the composition of the electrocoating bath that changes due to continuous electrocoating. If the change can be kept extremely small, and as a result, coated products of constant quality can be stably manufactured, one excellent effect can be obtained.
第1図及び第2図は、本発明の電着塗装装置の糸路を示
す一実施例の線図的構成説明図であり・一部断面図であ
る。
l・・・・・・電着塗装浴槽 λ・・・・・・陰
極3・・・・・・マスキ・ング ≠・・
・・・・陽極帯域!・・・・・・陰極帯域 t
・・・Z:・陰極塗装液貯槽7・・・・・・イオン交換
処理装置 r・・・・・・予 備 槽り・・・・・・限
外濾過装置
特許用原人 ハニー化成株式会社FIG. 1 and FIG. 2 are diagrammatic configuration explanatory views of an embodiment showing the yarn path of the electrodeposition coating apparatus of the present invention, and are partially sectional views. l...Electrodeposition coating bathtub λ...Cathode 3...Masking ≠...
...Anode band! ...Cathode band t
... Z: - Cathode coating liquid storage tank 7 ... Ion exchange treatment device r ... Reserve tank ... Ultrafiltration device original person for patent Honey Kasei Co., Ltd.
Claims (1)
キング材l二より陽極帯域と陰極帯域に区分した電着塗
装浴槽、(b)#極塗装液貯楕、(C)イオン交換処理
装置および(d)予備槽から成’)、(&)の陰極帯域
からの陰極塗装液を(9)の陰極塗装液貯槽に送給り、
(t))の貯槽がらの陰極塗装液を(C)のイオン交換
処理装置に移送L、(Q)からの低pH通過液を((1
)の予備槽又は(及び)(a)の電着塗装浴槽の陽極帯
域に移送する糸路を設けたことを特徴とする電着塗装装
置。 2(a)電着塗装浴槽内を樹脂分を透過するマスキング
材により陽極帯域と陰極帯域に区分した電着塗装浴槽、
(至)陰極塗装液貯槽、(C)イオン交換処理装置、(
d)予備槽および(8)限外濾過装置から成’)、(a
)の陰極帯域からの陰極塗装液を(1))の陰極塗装液
貯槽に送給り、(1))の貯槽がらの陰極塗装液を(e
)の限外濾過装置に移送し1濾過膜を透過しない渉厚液
は(至)の貯槽又は(及び)(a)の陽極帯域に戻し透
過液は(C)のイオン交換処理装置に移送し、(C)か
らの低pH通過液を((L)の予備槽又は(及び)(a
)の電着塗装浴槽の陽極帯域に移送する糸路を設けたこ
とを特徴とする電着塗装装置。[Scope of Claims] / (a) An electrodeposition coating bathtub divided into an anode zone and a cathode zone by a masking material that transmits resin inside the bathtub, (b) #polar coating liquid storage oval, (C) consisting of an ion exchange treatment device and (d) a reserve tank; sending the cathode coating liquid from the cathode zones of (&) to the cathode coating liquid storage tank of (9);
The cathode coating liquid from the storage tank (t) is transferred to the ion exchange treatment device (C) L, and the low pH passing liquid from (Q) is transferred to the ion exchange treatment device (C) ((1).
1. An electrocoating apparatus, characterized in that it is provided with a thread path for transporting it to the preparatory tank of () or the anode zone of the electrocoating bath of (a). 2(a) An electrodeposition coating bathtub in which the interior of the electrodeposition coating bathtub is divided into an anode zone and a cathode zone using a masking material that allows resin to pass through;
(To) Cathode coating liquid storage tank, (C) Ion exchange treatment device, (
d) a preliminary tank and (8) an ultrafiltration device;
The cathode coating liquid from the cathode zone of ) is sent to the cathode coating liquid storage tank of (1)), and the cathode coating liquid from the storage tank of (1)) is fed to the cathode coating liquid storage tank of (1)).
The thickened liquid that does not pass through the ultrafiltration device (1) is transferred to the storage tank (to) or (and) the anode zone (a), and the permeated liquid is transferred to the ion exchange treatment device (C). , (C) to the pre-tank of (L) or (and) (a
1.) Electrodeposition coating equipment, characterized in that it is provided with a thread path for transporting it to the anode zone of the electrodeposition coating bath.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56190095A JPS6010118B2 (en) | 1981-11-26 | 1981-11-26 | Electrodeposition coating equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56190095A JPS6010118B2 (en) | 1981-11-26 | 1981-11-26 | Electrodeposition coating equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5891199A true JPS5891199A (en) | 1983-05-31 |
JPS6010118B2 JPS6010118B2 (en) | 1985-03-15 |
Family
ID=16252280
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56190095A Expired JPS6010118B2 (en) | 1981-11-26 | 1981-11-26 | Electrodeposition coating equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6010118B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0262419A2 (en) * | 1986-09-03 | 1988-04-06 | BASF Aktiengesellschaft | Process for removing acids from cataphoretic painting baths |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6033127U (en) * | 1983-08-10 | 1985-03-06 | 札幌アルナ株式会社 | heating device |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4821338U (en) * | 1971-07-22 | 1973-03-10 | ||
JPS494538A (en) * | 1972-04-24 | 1974-01-16 |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3444066A (en) * | 1966-12-07 | 1969-05-13 | Ford Motor Co | Method of electrically induced deposition of paint on conductors |
-
1981
- 1981-11-26 JP JP56190095A patent/JPS6010118B2/en not_active Expired
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4821338U (en) * | 1971-07-22 | 1973-03-10 | ||
JPS494538A (en) * | 1972-04-24 | 1974-01-16 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0262419A2 (en) * | 1986-09-03 | 1988-04-06 | BASF Aktiengesellschaft | Process for removing acids from cataphoretic painting baths |
Also Published As
Publication number | Publication date |
---|---|
JPS6010118B2 (en) | 1985-03-15 |
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