JPH0280596A - Method and apparatus for coating shade-shaped article by electrodeposition - Google Patents
Method and apparatus for coating shade-shaped article by electrodepositionInfo
- Publication number
- JPH0280596A JPH0280596A JP22979588A JP22979588A JPH0280596A JP H0280596 A JPH0280596 A JP H0280596A JP 22979588 A JP22979588 A JP 22979588A JP 22979588 A JP22979588 A JP 22979588A JP H0280596 A JPH0280596 A JP H0280596A
- Authority
- JP
- Japan
- Prior art keywords
- coating
- electrodeposition
- coated
- electrodeposition coating
- coating liquid
- 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
Links
- 238000000576 coating method Methods 0.000 title claims abstract description 141
- 239000011248 coating agent Substances 0.000 title claims abstract description 138
- 238000004070 electrodeposition Methods 0.000 title claims abstract description 77
- 238000000034 method Methods 0.000 title description 6
- 229920000178 Acrylic resin Polymers 0.000 claims abstract description 5
- 239000004925 Acrylic resin Substances 0.000 claims abstract description 5
- 229920000877 Melamine resin Polymers 0.000 claims abstract description 5
- 239000004640 Melamine resin Substances 0.000 claims abstract description 4
- 239000007788 liquid Substances 0.000 claims description 55
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 8
- 239000002932 luster Substances 0.000 abstract 2
- 239000003973 paint Substances 0.000 description 12
- 229910001220 stainless steel Inorganic materials 0.000 description 11
- 239000010935 stainless steel Substances 0.000 description 11
- 239000008399 tap water Substances 0.000 description 7
- 235000020679 tap water Nutrition 0.000 description 7
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 6
- 230000005856 abnormality Effects 0.000 description 6
- 229910052782 aluminium Inorganic materials 0.000 description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 6
- 238000001035 drying Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 125000000129 anionic group Chemical group 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- SHZIWNPUGXLXDT-UHFFFAOYSA-N ethyl hexanoate Chemical compound CCCCCC(=O)OCC SHZIWNPUGXLXDT-UHFFFAOYSA-N 0.000 description 3
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000010422 painting Methods 0.000 description 3
- SOGAXMICEFXMKE-UHFFFAOYSA-N Butylmethacrylate Chemical compound CCCCOC(=O)C(C)=C SOGAXMICEFXMKE-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 2
- 229910052753 mercury Inorganic materials 0.000 description 2
- -1 polypropylene Polymers 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- ZOKCNEIWFQCSCM-UHFFFAOYSA-N (2-methyl-4-phenylpent-4-en-2-yl)benzene Chemical compound C=1C=CC=CC=1C(C)(C)CC(=C)C1=CC=CC=C1 ZOKCNEIWFQCSCM-UHFFFAOYSA-N 0.000 description 1
- DURPTKYDGMDSBL-UHFFFAOYSA-N 1-butoxybutane Chemical compound CCCCOCCCC DURPTKYDGMDSBL-UHFFFAOYSA-N 0.000 description 1
- BQTPKSBXMONSJI-UHFFFAOYSA-N 1-cyclohexylpyrrole-2,5-dione Chemical compound O=C1C=CC(=O)N1C1CCCCC1 BQTPKSBXMONSJI-UHFFFAOYSA-N 0.000 description 1
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- OBETXYAYXDNJHR-UHFFFAOYSA-N 2-Ethylhexanoic acid Chemical compound CCCCC(CC)C(O)=O OBETXYAYXDNJHR-UHFFFAOYSA-N 0.000 description 1
- POAOYUHQDCAZBD-UHFFFAOYSA-N 2-butoxyethanol Chemical compound CCCCOCCO POAOYUHQDCAZBD-UHFFFAOYSA-N 0.000 description 1
- 229920003270 Cymel® Polymers 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- WOBHKFSMXKNTIM-UHFFFAOYSA-N Hydroxyethyl methacrylate Chemical compound CC(=C)C(=O)OCCO WOBHKFSMXKNTIM-UHFFFAOYSA-N 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000007665 sagging Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 229920006305 unsaturated polyester Polymers 0.000 description 1
Landscapes
- Application Of Or Painting With Fluid Materials (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、特に半球形、筒形、錐形または帽子状等の笠
状あるいは椀状物品に、電着塗膜を形成する方法および
その方法を実施するための電着塗装装置に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for forming an electrodeposited coating film on a cap-shaped or bowl-shaped article such as a hemispherical, cylindrical, conical, or hat-shaped article, and a method thereof. The present invention relates to an electrocoating device for carrying out the method.
(従来の技術)
大型水銀灯など照明器具の反射板、自動車のライト部分
、パラボラアンテナ等、凹凸部分を有する物品に対し、
電着塗装を行うことが多い。これら物品に対する塗装は
、その機能上類して凸部より凹部(内面側)が重視され
、仕上り外観はもちろんのこととして、耐候性、耐薬品
性、耐傷付き性など、可成りハイレベルな諸性能が要求
されていた。(Prior art) For articles with uneven parts, such as reflectors of lighting equipment such as large mercury lamps, light parts of automobiles, and parabolic antennas,
Electrodeposition coating is often used. In terms of functionality, the coating of these items places more emphasis on concave areas (inner surfaces) than convex areas, and requires not only the finished appearance but also a fairly high level of weather resistance, chemical resistance, scratch resistance, etc. Performance was required.
(発明が解決しようとする課題)
従来、建材等の電着塗装を行っていた方法や装置(例え
ば実公昭47−38587号公報参照)を用いて、前記
の笠状物品に電着塗装を施した場合には、塗料の付き廻
り性が悪く、該物品に要求される前記の諸性能を満足さ
せることは、到底不可能であった。(Problem to be Solved by the Invention) Electrodeposition coating is applied to the above-mentioned shade-shaped article using the method and apparatus that have conventionally applied electrodeposition coating to building materials, etc. (see, for example, Japanese Utility Model Publication No. 47-38587). In this case, the paint coverage was poor and it was completely impossible to satisfy the above-mentioned performance requirements for the article.
前記した笠状物品には、特にその凹面側に均一でスムー
スな塗膜の形成が望まれるが、従来の塗装方法、塗装設
備を用いて電着塗装しても、泡、ムラ、タレなどの塗膜
外観不良を抑えることができず、塗膜の光沢、反射率が
劣っていた。It is desired that a uniform and smooth coating film be formed on the above-mentioned hat-shaped articles, especially on the concave side, but even if electrodeposition is applied using conventional coating methods and coating equipment, bubbles, unevenness, sagging, etc. will occur. It was not possible to suppress defects in the appearance of the paint film, and the gloss and reflectance of the paint film were poor.
本発明は、上記した従来技術による欠点を解消した、特
に笠状物品への電着塗装方法ならびに電着塗装装置を提
供することを目的としている。It is an object of the present invention to provide a method and apparatus for electrodeposition coating, particularly for a shade-shaped article, which eliminates the drawbacks of the prior art described above.
なお、本発明は被塗装物の形状が前記のものに限られる
訳ではなく、その他の形状の物品にも通用は可能である
。Note that the present invention is not limited to the shape of the object to be coated as described above, and can be applied to articles of other shapes as well.
(課題を解決するための手段)
上記目的を達成するために、本発明は、アクリル、メラ
ミン樹脂を塗膜形成主成分とする電着塗装液を使用し、
内外壁面に接する塗装液を電気的に導通させるようにし
た内筒と、外筒より構成されている二重筒構造を有する
電着塗装用槽に電着塗装液を満たすと共に内筒内側に被
塗装物を浸漬し、内、外筒間あるいは内筒内側に対極を
設けて、前記被塗装物と対極との間に電圧を印加するこ
とにより、被塗物上に塗膜を析出形成せしめるものであ
る。(Means for Solving the Problems) In order to achieve the above object, the present invention uses an electrodeposition coating liquid containing acrylic and melamine resin as main components for forming a coating film,
An electrodeposition coating tank having a double-tube structure consisting of an inner cylinder and an outer cylinder, which are designed to electrically conduct the coating liquid in contact with the inner and outer walls, is filled with the electrodeposition coating liquid, and the inside of the inner cylinder is coated. A coating film is deposited and formed on the object by dipping the object to be coated, providing a counter electrode between the inner and outer cylinders, or inside the inner cylinder, and applying a voltage between the object and the counter electrode. It is.
(作用)
上記のように構成された本発明により、笠状物品に対し
て電着塗装を実施したところ、大型の被塗装物の、特に
凹面側に対して塗料の付き廻り性に優れ、均一でスムー
スな塗膜が形成され、電着塗装のメリットを最大限に活
用することができた。(Function) When electrodeposition coating was performed on a cap-shaped article according to the present invention configured as described above, the paint coverage was excellent and uniform, especially on the concave side of a large object. A smooth coating film was formed and the benefits of electrodeposition coating could be utilized to the fullest.
(実施例)
実施例について、図面を参照して説明すると、第1図〜
第3図(イ)(ロ)は、本発明の電着塗装装置の主要構
造を示している。外筒1および内筒2の中間に被塗装物
に対する対極4が設けられている。内筒2にはその両側
の電着塗装液を電気的に導通させると共に塗装液が流通
するための通孔3が備えられる。対極4上にも、前記通
孔3に対応する部分には、通孔5が設けられて、塗装液
を流通せしめるようになっている。内、外筒間の上部に
は、電着塗装槽への塗装液流入管6が、槽全周にわたっ
て配置される。他方、内筒内側下部には、塗装液流出管
7が内筒に同心的に配置される。流入管6および流出管
7の下側には、塗料液の出入りする穴6′、6″、6″
・・・・、7′、7.7″・・・・を適宜間隔で設ける
。(Example) An example will be explained with reference to the drawings.
Figures 3(a) and 3(b) show the main structure of the electrodeposition coating apparatus of the present invention. A counter electrode 4 for the object to be coated is provided between the outer cylinder 1 and the inner cylinder 2. The inner cylinder 2 is provided with a through hole 3 for electrically conducting the electrodeposition coating liquid on both sides thereof and for the coating liquid to flow therethrough. A through hole 5 is also provided on the counter electrode 4 at a portion corresponding to the through hole 3 to allow the coating liquid to flow therethrough. In the upper part between the inner and outer cylinders, a coating liquid inflow pipe 6 to the electrodeposition coating tank is arranged around the entire circumference of the tank. On the other hand, at the inner lower part of the inner cylinder, a coating liquid outflow pipe 7 is arranged concentrically with the inner cylinder. At the bottom of the inflow pipe 6 and outflow pipe 7, there are holes 6', 6'', 6'' through which the paint liquid enters and exits.
..., 7', 7.7'', etc. are provided at appropriate intervals.
第4図および第5図(イ)は、代表的な被塗装物8の平
面図および同(ロ)は側面断面図を示すものである。被
塗装物8は、通常リード線10を備えた通電用接点の役
割をなすハンガー9で塗装液中に支持される。FIGS. 4 and 5 (a) show a plan view of a typical object to be coated 8, and FIG. 5 (b) shows a side sectional view. The object to be painted 8 is supported in the coating liquid by a hanger 9 that is normally equipped with a lead wire 10 and serves as a current-carrying contact.
第6図は、電着塗装の実施状況を示すものである。塗装
液流入管6より電着塗装槽に送入された塗装液は、対極
4および内筒2の通孔3および同5を通過して、槽内に
満たされる。内筒2内下部にffi、Qけた塗装液流出
管7は、その下部に孔7′、7n 、7n・・・・が必
るため、該孔に吸込まれる塗装液により、被塗装物8の
内周辺には矢印へで示すような循環流が生ずる。このよ
うな状態で、被塗装物8をハンガー9によって電着塗装
槽の内筒内側に懸吊し、リード線10を正極に、対極5
を負極に接続して電圧を印加する。上記した流出管7に
より生じた塗装液の循環流は、電着塗装により発生する
塗料成分の不均一を補償し、均一な塗膜を形成するのに
役立っている。FIG. 6 shows the implementation status of electrodeposition coating. The coating liquid fed into the electrodeposition coating tank from the coating liquid inlet pipe 6 passes through the counter electrode 4 and the through holes 3 and 5 of the inner cylinder 2, and fills the tank. The coating liquid outflow pipe 7 with ffi and Q girders in the lower part of the inner cylinder 2 has holes 7', 7n, 7n, etc. in its lower part, so the coating liquid sucked into the holes can cause the coating liquid to flow through the object 8. Circulating flow occurs around the inside as shown by the arrow. In this state, the object to be coated 8 is suspended inside the inner cylinder of the electrodeposition coating tank by the hanger 9, the lead wire 10 is connected to the positive electrode, and the counter electrode 5 is connected to the electrode 5.
Connect to the negative pole and apply voltage. The circulating flow of the coating liquid generated by the above-mentioned outflow pipe 7 serves to compensate for non-uniformity of coating components caused by electrodeposition coating and to form a uniform coating film.
電着塗装用槽(内、外筒と底部)はステンレス鋼、ポリ
プロピレン、硬質塩化ビニル、不飽和ポリエステルなど
を用いて作製することができる。The electrocoating tank (inner and outer cylinders and bottom) can be made of stainless steel, polypropylene, hard vinyl chloride, unsaturated polyester, or the like.
対極としては、ステンレス鋼、チタンなど耐食性に優れ
た金属が適している。槽をステンレス鋼で作製した場合
には、槽壁を対極として使用することもできる。また、
槽の断面形状は、円形、楕円形、角形等いずれにも限定
されないが、均一な塗膜形成には、被塗装物8の断面と
相似させるのが理想的である。As the counter electrode, metals with excellent corrosion resistance such as stainless steel and titanium are suitable. If the tank is made of stainless steel, the tank wall can also be used as a counter electrode. Also,
Although the cross-sectional shape of the tank is not limited to any of circular, elliptical, and square shapes, it is ideal to have a cross-sectional shape similar to the cross-section of the object 8 to be coated in order to form a uniform coating film.
電着塗装においては、通常塗装中は塗装液は循環を止め
るか、極微量の循環下で行うのが好ましい。これは、形
成された塗膜が、塗料液の流れによって塗膜の剥離や外
観の劣化を防止するためである。しかし、本発明におい
ては、必要があれば塗装液の循環を行うが、電着塗装槽
内での塗装液の流れは、内筒2内側に設けた流出管の下
側から塗装液を吸込み、内、外筒間上部の流入管6から
流入させるのが好ましい。この際、配管内での流速、あ
るいは流量を限定する必要はない。また、循環経路の途
中に、塗料液温度調節用の熱交換器、フィルター等を設
ければ、ざらに優れた効果が奏される。In electrodeposition coating, it is usually preferable to stop the circulation of the coating liquid during coating or to carry out circulation in a very small amount. This is to prevent the formed coating film from peeling off or deteriorating its appearance due to the flow of the coating liquid. However, in the present invention, although the coating liquid is circulated if necessary, the flow of the coating liquid in the electrodeposition coating tank is such that the coating liquid is sucked in from the bottom of the outflow pipe provided inside the inner cylinder 2. It is preferable to flow in from the inflow pipe 6 located above the space between the inner and outer cylinders. At this time, there is no need to limit the flow rate or flow rate within the pipe. Moreover, if a heat exchanger, filter, etc. for controlling the temperature of the paint liquid is provided in the middle of the circulation path, even better effects can be achieved.
本発明の具体的操業例は、次の通りである。A specific operation example of the present invention is as follows.
実施例1
(実施例1で用いる電着塗装液の調製)温度計、撹拌機
および還流冷却器を備えた11四つロフラスコに、エチ
レング(ノコールモノブチルエーテル 2509、ター
シャリ−ブチルパーオキシ−2−エチルヘキサノエート
7.57を仕込み、80℃に昇温する。これにメタク
リル酸メチル 131g、メタクリル酸n−ブチル 9
0g、アクリル酸エチル 410g、アクリル酸14り
、メタクリル酸2−ヒドロキシエチル 80g、N−シ
クロへキシルマレイミド 75g、2.4−ジフェニル
−4−メチル−1−ペンテン1gの単量体混合物を、2
40分間にかけてフラスコ内に滴下した俊、ざらに24
0分間撹拌を行う。ついで、エチレングリコールモノブ
チルエテル 30g、ターシャリ−ブチルパーオキシ−
2−エチルヘキサノエート 1.5gの混合物を60分
毎に3回添加する。その後80℃で240分間撹拌を続
はアニオン系アクリル樹脂を調製した。Example 1 (Preparation of electrodeposition coating solution used in Example 1) Into a 11-four-bottom flask equipped with a thermometer, a stirrer, and a reflux condenser, ethylene (nocol monobutyl ether 2509, tert-butyl peroxy-2- Charge 7.57 g of ethylhexanoate and raise the temperature to 80°C.To this, 131 g of methyl methacrylate and 9 g of n-butyl methacrylate.
A monomer mixture of 0 g, 410 g of ethyl acrylate, 14 g of acrylic acid, 80 g of 2-hydroxyethyl methacrylate, 75 g of N-cyclohexylmaleimide, and 1 g of 2,4-diphenyl-4-methyl-1-pentene was mixed with 2
Shun, Zaraani 24 dripped into the flask over 40 minutes
Stir for 0 minutes. Next, 30 g of ethylene glycol monobutyl ether, tertiary butyl peroxy
2-Ethylhexanoate 1.5 g of the mixture is added three times every 60 minutes. Thereafter, the mixture was stirred at 80° C. for 240 minutes to prepare an anionic acrylic resin.
つぎに容器にこのアニオン系アクリル樹脂 120g、
メラミン樹脂(商品名サイメルHM−6三井サイアナミ
ツド社製> 309を採取し、十分に撹拌を行い、ざ
らにト1ノエチルアミンを添加し十分に撹拌を行った。Next, put 120g of this anionic acrylic resin in a container.
Melamine resin (trade name: Cymel HM-6, manufactured by Mitsui Cyanamid Co., Ltd.> 309) was collected and thoroughly stirred, and 1-noethylamine was added to the colander and thoroughly stirred.
ついで撹拌しながらイオン交換水を徐々に加え、樹脂固
形分約10重量%の電着塗装液を調製した。Then, ion-exchanged water was gradually added while stirring to prepare an electrodeposition coating solution having a resin solid content of about 10% by weight.
第1図に示す内筒径500m、外筒径600#、深さ5
80Mの二重筒構造のアクリル製電着塗装槽を用いて、
第5図に示す形状のアルミニウム被塗物の電着塗装を行
った。 内筒外壁上部および中央部に沿って円形に硬質
塩化ビニル製塗装液流出管、同じく内筒底部に円形に硬
質塩化ビニル製塗装液流出管を装着し、内筒管底部より
280m、40Mの周上に直径80mの穴を6個ずつ等
間隔に設け、内筒内と内、外筒間の塗装液の循環を60
1/分の速度で行った。Inner cylinder diameter 500m, outer cylinder diameter 600#, depth 5 as shown in Figure 1
Using an acrylic electrodeposition coating tank with a double cylinder structure of 80M,
An aluminum object having the shape shown in FIG. 5 was electrodeposited. A hard vinyl chloride coating liquid outflow pipe is installed in a circular manner along the top and center of the outer wall of the inner cylinder, and a hard vinyl chloride paint liquid outflow pipe is also installed in a circular manner at the bottom of the inner cylinder. Six holes with a diameter of 80 m are provided at equal intervals on the top, and the circulation of the coating liquid between the inner cylinder and the inner and outer cylinders is made 60 m in diameter.
This was done at a speed of 1/min.
前記電着塗装液を用い、被塗物を陽極に、内筒内面に沿
ってほぼ等間隔にさし入れた12枚のステンレス板(6
01MX500mInX0.5IIa>を陰極に接続し
、電着塗装を行った。Using the above electrodeposition coating liquid, 12 stainless steel plates (6
01MX500mInX0.5IIa> was connected to the cathode, and electrodeposition coating was performed.
電着塗装は、液温25℃、印加電圧60V、通電時間3
分直流通電を行った。ついで被塗物を引き上げ、水道水
で十分水洗した後、180℃で20分焼付は乾燥を行っ
た。この結果、塗膜外観は、ピンホール・傷・泡などの
異常はなく、塗膜厚も12〜13μmで均一でスムース
な塗膜が形成できた。For electrodeposition coating, the liquid temperature is 25℃, the applied voltage is 60V, and the energization time is 3.
A branch direct current was applied. The object to be coated was then taken out, thoroughly washed with tap water, and then baked and dried at 180° C. for 20 minutes. As a result, the coating film had no abnormalities such as pinholes, scratches, or bubbles, and a uniform and smooth coating film with a coating thickness of 12 to 13 μm was formed.
実施例2
第2図に示す内筒径110m、外筒径150m、深さ1
40mの二重筒構造のアクリル製電着塗装用槽を用いて
、第4図に示す形状のアルミニウム被塗物の電着塗装を
行った。Example 2 Inner cylinder diameter 110 m, outer cylinder diameter 150 m, depth 1 as shown in Fig. 2
An aluminum object having the shape shown in FIG. 4 was electrocoated using a 40 m double-tube acrylic electrocoating tank.
内筒側面に底面より40mの円周上に直径20mの穴を
等間隔に4個設け、内筒内部底面と、内、外筒間上部に
硬質塩化ビニルパイプを装着し、内筒と、外筒間の塗装
液の循環を101/分の速度で行った。Four holes with a diameter of 20 m are provided at equal intervals on the circumference of the inner cylinder at a distance of 40 m from the bottom surface, and hard vinyl chloride pipes are attached to the inner bottom of the inner cylinder and the upper part between the inner and outer cylinders. The coating liquid was circulated between the cylinders at a rate of 101/min.
電着塗装法は市販のアクリル−メラミン系電着塗装液(
商品名ハニブライトC−1ハニー化成株式会社製)を用
い、被塗物を陽極に、内、外筒間にほぼ等間隔にざし入
れた4枚のステンレス板(30x1ooxo、2#l)
を陰極に接続し、電圧を印加しアニオン電着塗装を行っ
た。The electrodeposition coating method uses a commercially available acrylic-melamine electrodeposition coating liquid (
Four stainless steel plates (30 x 10oxo, 2#l) were inserted at approximately equal intervals between the inner and outer cylinders, using the product to be coated as the anode (product name Honeybright C-1 manufactured by Honey Kasei Co., Ltd.).
was connected to the cathode, voltage was applied, and anion electrodeposition coating was performed.
電着塗装は、液温25℃、印加電圧100v、通電時間
3分直流通電を行った。ついで、水道水で十分に水洗し
、10分間常温で放置した。その後、180℃で20分
間焼付は乾燥を行った。Electrodeposition coating was carried out at a liquid temperature of 25° C., an applied voltage of 100 V, and a direct current flow for 3 minutes. Then, it was thoroughly washed with tap water and left at room temperature for 10 minutes. Thereafter, baking and drying were performed at 180° C. for 20 minutes.
塗装仕上がり状態を目視で判定し、塗膜厚を市販の膜厚
計(商品名パーマスコープフィッシャー社製)で測定し
た。この結果、塗膜外観は、ピンホール・傷・泡などの
異常はなく、塗膜厚も9〜10μmで均一でスムースな
電着塗膜が形成できた。The finished state of the coating was visually determined, and the coating film thickness was measured using a commercially available film thickness meter (trade name: Permascope Fisher Co., Ltd.). As a result, the coating film had no abnormalities such as pinholes, scratches, or bubbles, and a uniform and smooth electrodeposited coating film with a coating thickness of 9 to 10 μm was formed.
実施例3
実施例2と同じ形状の電着塗装槽、および同じ形状のア
ルミニウム被塗物を用い、電着塗装液として市販のアク
リル系電着塗料(商品名ニレコートCM 株式会社シミ
ズ製)を用いて、被塗物を陰極に、内、外筒間に設けた
ステンレス板を陽極に接続し、カチオン電着塗装を行っ
た。 電着塗装は、液温30℃、印加電圧50V、通電
時間3分直流通電件を行った。ついで水道水で十分に水
洗し、10分間常温で放置した。その後、遠赤外線照射
下160℃で20分間焼付は乾燥を行った。Example 3 Using an electrodeposition coating tank with the same shape as in Example 2 and an aluminum coating object with the same shape, a commercially available acrylic electrodeposition paint (trade name Nirecoat CM, manufactured by Shimizu Co., Ltd.) was used as the electrodeposition coating liquid. Then, cationic electrodeposition was performed by connecting the object to be coated as a cathode and the stainless steel plate provided between the inner and outer cylinders as an anode. Electrodeposition coating was performed under direct current conditions at a liquid temperature of 30° C., an applied voltage of 50 V, and a current application time of 3 minutes. Then, it was thoroughly washed with tap water and left at room temperature for 10 minutes. Thereafter, baking and drying were performed at 160° C. for 20 minutes under far infrared irradiation.
この結果、塗膜外観は、ピンホール・傷・泡などの異常
はなく、被塗物の塗膜厚も13〜15μ而で均一でスム
ースな電着塗膜が形成できた。実施例4
実施例3と同じ形状の電着塗装槽、および同じ電着塗装
液を用いて、被塗物としてステンレス板(SUS 30
4 :300x400x2m>にアニオン電着塗装を
行った。As a result, there were no abnormalities such as pinholes, scratches, or bubbles in the appearance of the coating, and a uniform and smooth electrodeposited coating with a coating thickness of 13 to 15 μm on the object to be coated was formed. Example 4 A stainless steel plate (SUS 30
4: Anionic electrodeposition coating was applied to the area of 300 x 400 x 2 m.
電着塗装は、液温25℃、印加電圧50V、通電時間3
分直流通電を行った。ついで水通水で十分に水洗した後
、150℃で20分焼付は乾燥を行った。この結果、塗
膜外観は、ピンホール・傷・泡などの異常はなく、塗膜
厚も18〜20μ汎で均一でスムースな電着塗膜が形成
できた。For electrodeposition coating, the liquid temperature is 25℃, the applied voltage is 50V, and the energization time is 3.
A branch direct current was applied. Then, after thoroughly washing with running water, baking and drying were performed at 150° C. for 20 minutes. As a result, the coating film had no abnormalities such as pinholes, scratches, or bubbles, and a uniform and smooth electrodeposited coating film with a coating thickness of 18 to 20 μm was formed.
実施例5
実施例3と同じ形状の電着塗装槽、および同じ電着塗装
液を用いて、被塗物として鉄板(JISG 3141
:300X300X2m>にアニオン電着塗装を行った
。Example 5 Using an electrodeposition coating tank with the same shape and the same electrodeposition coating solution as in Example 3, an iron plate (JISG 3141
:300X300X2m> was subjected to anion electrodeposition coating.
電着塗装は、液温25℃、印加電圧50V、通電時間3
分直流通電を行った。ついで水道水で十分に水洗した優
、150℃で20分焼付は乾燥を行った。この結果、塗
膜外観は、ピンホール・傷・泡などの異常はなく、塗膜
厚も18〜20μ面で均一でスムースな電着塗膜が形成
できた。For electrodeposition coating, the liquid temperature is 25℃, the applied voltage is 50V, and the energization time is 3.
A branch direct current was applied. Then, it was washed thoroughly with tap water, baked at 150° C. for 20 minutes, and dried. As a result, the coating film had no abnormalities such as pinholes, scratches, or bubbles, and a uniform and smooth electrodeposited coating film with a coating thickness of 18 to 20 μm was formed.
実施例6
第3図に示す二重六角形筒型構造のエポキシ樹脂でライ
ニングを施したステンレス製電着塗装槽を用いて、第5
図に示す形状のアルミニウム被塗物の電着塗装を行った
。Example 6 Using a stainless steel electrodeposition coating tank lined with epoxy resin and having a double hexagonal cylindrical structure shown in FIG.
Electrodeposition coating was performed on an aluminum object having the shape shown in the figure.
内筒外壁上部および中央部に円形に硬質塩化ビニル製塗
装液流出管を装着し、内筒側面中央および下方に接して
の円周上に直径80sの穴を6個づつ等間隔に開け、内
筒と内、外筒間の塗装液の循環を6017分の速度で行
った。Attach a circular hard vinyl chloride coating liquid outflow pipe to the top and center of the outer wall of the inner cylinder, and drill six holes with a diameter of 80 s at equal intervals on the circumference in contact with the center and bottom side of the inner cylinder. The coating liquid was circulated between the cylinder and the inner and outer cylinders at a speed of 6017 minutes.
実施例1で使用した電着塗装液を用い、被塗物を陽極に
内筒内面に沿ってほぼ等間隔にさし入れた12枚のステ
ンレス板(100x500x0゜5 m >を陰極に接
続し電着塗装を行ったII!塗装は25℃、印加電圧6
0v1通電時間3分直流通電を行った。ついで水道水で
十分水洗し、10分間常温で放置した。その後、180
℃で20分焼付は乾燥を行った。この結果、塗膜外観は
、ピンホール・傷・泡などの異常はなく、塗膜厚も12
〜13μmで均一でスムースな電着塗膜が形成できた。Using the electrodeposition coating liquid used in Example 1, 12 stainless steel plates (100 x 500 x 0゜5 m) were inserted into the anode at approximately equal intervals along the inner surface of the inner cylinder and connected to the cathode. Painting was done II! Painting was done at 25℃ and applied voltage 6
Direct current was applied for 3 minutes at 0v1 current. Then, it was thoroughly washed with tap water and left at room temperature for 10 minutes. After that, 180
Baking was performed at ℃ for 20 minutes to dry. As a result, there were no abnormalities such as pinholes, scratches, or bubbles in the appearance of the paint film, and the film thickness was 12.
A uniform and smooth electrodeposition coating film with a thickness of ~13 μm could be formed.
比較例1
第7図に示すアクリル製電着塗装槽を用いて、第5図に
示す形状のアルミニウム被塗物の電着塗装を行った。Comparative Example 1 An acrylic electrodeposition coating tank shown in FIG. 7 was used to electrocoat an aluminum object having the shape shown in FIG. 5.
水槽底部に電着塗装液吹き出し用、オーバーフロー槽底
部に電着塗装液吸い込み用の硬質塩化ビニルパイプを装
着し、水槽からオーバーフロー槽へ電着塗装液を101
/分の速度でオーバーフローさせ循環した。Attach a hard PVC pipe to the bottom of the water tank for blowing out the electrodeposition coating liquid and to the bottom of the overflow tank for sucking the electrodeposition coating liquid.
It was overflowed and circulated at a rate of 1/min.
実施例1で使用した電着塗装液を用い、被塗物を陽極に
、水槽内壁両側にほぼ等間隔に2枚ずつさし入れたステ
ンレス板(50x120x0.5M)を陰極に接続し、
電着塗装を行った。Using the electrodeposition coating solution used in Example 1, the object to be coated was connected to the anode, and two stainless steel plates (50 x 120 x 0.5M) inserted at approximately equal intervals on both sides of the inner wall of the water tank were connected to the cathode.
Electrodeposition painting was performed.
電着塗装は、液温25℃、印加電圧60V、通電時間3
分直流通電を行った。ついで水道水で+分水洗した後、
180℃で20分焼付は乾燥を行った。この結果、塗膜
外観は、泡・ムラが発生し、塗膜厚も5〜15μ而と不
均一な電着塗膜が形成された。For electrodeposition coating, the liquid temperature is 25℃, the applied voltage is 60V, and the energization time is 3.
A branch direct current was applied. Then, after washing with tap water,
Baking and drying were performed at 180° C. for 20 minutes. As a result, bubbles and unevenness occurred in the coating film appearance, and an uneven electrodeposited coating film was formed with a coating thickness of 5 to 15 μm.
比較例2
第8図に示す角型二重構造のアクリル製電着塗装槽を用
いて、第4図に示す形状のアルミニウム被塗物の電着塗
装を行った。Comparative Example 2 An aluminum object having the shape shown in FIG. 4 was electrodeposited using a rectangular double-structure acrylic electrodeposition coating tank shown in FIG.
内槽底部に電着塗装液吸き出し用、外槽開底部に電着塗
装液吸い込み用の硬質塩化ビニルパイプを装着し、内槽
から外槽ヘオーバーフローさせ6017分の速度で塗装
液を循環した。A hard vinyl chloride pipe is installed at the bottom of the inner tank for sucking out the electrodeposition coating liquid, and at the open bottom of the outer tank for sucking the electrodeposition coating liquid, and the coating liquid is circulated at a speed of 6017 minutes by overflowing from the inner tank to the outer tank. did.
実施例1で使用した電着塗装液を用い、被塗物を陽極に
、内槽内壁両側にほぼ等間隔に3枚ずつざし入れたステ
ンレス板(100X500x0゜5 m >を陰極に接
続し、電着塗装を行った。Using the electrodeposition coating liquid used in Example 1, with the object to be coated as the anode, three stainless steel plates (100 x 500 x 0゜5 m) placed at approximately equal intervals on both sides of the inner wall of the inner tank were connected to the cathode. I applied a coat of paint.
電着塗装は、液温25℃、印加電圧70V、通電時間3
分直流通電を行った。ついで水道水で十分水洗し、10
分間常温で放置した。その後、180℃で20分焼付は
乾燥を行った。この結果、塗膜外観は、クレータ・ゴミ
付着が発生し、塗膜厚も8〜20μmと不均一な電着塗
膜が形成された。For electrodeposition coating, the liquid temperature is 25℃, the applied voltage is 70V, and the energization time is 3.
A branch direct current was applied. Next, wash thoroughly with tap water,
It was left at room temperature for a minute. Thereafter, baking and drying were performed at 180° C. for 20 minutes. As a result, the appearance of the coating film showed craters and dust adhesion, and an uneven electrodeposition coating film was formed with a coating thickness of 8 to 20 μm.
(発明の効果)
本発明は、以上説明したように構成されているので、以
下に記載されるような効果を奏する。(Effects of the Invention) Since the present invention is configured as described above, it produces effects as described below.
本発明によれば、従来、電着塗装では均一な塗膜を形成
することが困難であった大型笠状物品、例えば大型水銀
灯の反射板の凹面部表面にも、均一でスムース、かつ耐
候性、耐薬品性、耐傷付き性および光沢、反射率のいず
れにも充分な特性を示す電着塗膜が形成される。また、
本発明の電着塗装装置は、N@塗装液の損失、劣化が少
なく、連続して均一でスムースな電着塗装を長期間にわ
たり実施することができる。According to the present invention, it is possible to apply a uniform, smooth, and weather-resistant coating even to the concave surface of a large shade-shaped article such as a reflector of a large mercury lamp, for example, where it has been difficult to form a uniform coating film using electrodeposition coating. An electrodeposited coating film is formed which exhibits sufficient properties in terms of chemical resistance, scratch resistance, gloss, and reflectance. Also,
The electrodeposition coating apparatus of the present invention causes less loss and deterioration of the N@ coating solution, and can continuously perform uniform and smooth electrodeposition coating over a long period of time.
第1図、第2図および第3図の(イ)は本発明電着塗装
置の主要部を示す平面図、同(ロ)は側面断面図、第4
図および第5図(イ)は、代表的な笠状被塗装物にの平
面図、同(ロ)は側面断面図、第6図は、本発明の操作
状態を示す側面断面図、第7図および第8図(イ)は、
従来の電着塗装装置の主要部を示す平面図、同(ロ)は
側面断面図でおる。
外 筒
内 筒
通 孔
対 極
対極上の通孔
10゜
塗料液流入管
塗料液流出管
被塗装物
電気接点
兼用ハンガー
リード線
第1図1, 2, and 3 (a) are plan views showing the main parts of the electrodeposition coating apparatus of the present invention, (b) are side sectional views, and (4)
5 and 5(a) are a plan view of a typical shade-shaped object to be coated, FIG. 5(b) is a side sectional view, FIG. The figure and Figure 8 (a) are
FIG. 2 is a plan view showing the main parts of a conventional electrodeposition coating device, and (b) is a side sectional view. Outer Cylinder Inner Cylinder Through Hole Pair Pole Pole Through hole on the pole 10° Paint liquid inflow tube Paint liquid outflow tube Hanger lead wire that also serves as electrical contact for the object to be coated Figure 1
Claims (2)
液を使用し、笠状物品を電着塗装するに際し、内外壁面
に接する電着塗装液を電気的に導通させるようにした内
筒と、外筒より構成されている二重筒構造の電着塗装用
槽内に前記塗装液を満たし、内筒内側に被塗装物を浸漬
し、内筒内側あるいは内、外筒間の塗装液内に対極を設
けて、被塗装物と前記対極間に電圧を印加し、被塗装物
上に塗膜を形成することよりなる電着塗装方法。(1) When electrocoating a hat-shaped article using an electrocoating liquid containing acrylic or melamine resin as the main component, an inner cylinder is designed to electrically conduct the electrocoating liquid in contact with the inner and outer walls. , fill the coating liquid in a double-tube electrodeposition coating tank consisting of an outer cylinder, immerse the object to be coated inside the inner cylinder, and place the coating liquid inside the inner cylinder or between the inner and outer cylinders. An electrodeposition coating method comprising: providing a counter electrode to the object to be coated, and applying a voltage between the object to be coated and the counter electrode to form a coating film on the object to be coated.
、内筒はその両壁面に接する塗装液を電気的に導通する
構造を備え、内外筒間の上部に塗装液の流入導管を、ま
た内筒内の下部に塗装液の流出管を設けると共に、内、
外筒間あるいは内筒内壁近傍に被塗装物に対する荷電用
対極を設けてなる笠状物品の電着塗装用装置。(2) Consisting of a double cylinder that stores the electrodeposition coating liquid in the internal space, the inner cylinder has a structure that electrically conducts the coating liquid that is in contact with both walls, and an inflow conduit for the coating liquid is provided at the upper part between the inner and outer cylinders. In addition, an outflow pipe for the coating liquid is provided at the bottom of the inner cylinder, and
An apparatus for electrodeposition coating of a cap-shaped article, which is provided with a counter electrode for charging the object to be coated between the outer cylinders or near the inner wall of the inner cylinder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22979588A JPH0280596A (en) | 1988-09-16 | 1988-09-16 | Method and apparatus for coating shade-shaped article by electrodeposition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22979588A JPH0280596A (en) | 1988-09-16 | 1988-09-16 | Method and apparatus for coating shade-shaped article by electrodeposition |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0280596A true JPH0280596A (en) | 1990-03-20 |
Family
ID=16897793
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP22979588A Pending JPH0280596A (en) | 1988-09-16 | 1988-09-16 | Method and apparatus for coating shade-shaped article by electrodeposition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0280596A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010023839A (en) * | 2009-11-05 | 2010-02-04 | Nsk Ltd | Hub unit bearing and electrodeposition coating method of the same |
-
1988
- 1988-09-16 JP JP22979588A patent/JPH0280596A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010023839A (en) * | 2009-11-05 | 2010-02-04 | Nsk Ltd | Hub unit bearing and electrodeposition coating method of the same |
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