JPS6350880B2 - - Google Patents
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- Publication number
- JPS6350880B2 JPS6350880B2 JP54137303A JP13730379A JPS6350880B2 JP S6350880 B2 JPS6350880 B2 JP S6350880B2 JP 54137303 A JP54137303 A JP 54137303A JP 13730379 A JP13730379 A JP 13730379A JP S6350880 B2 JPS6350880 B2 JP S6350880B2
- Authority
- JP
- Japan
- Prior art keywords
- printed wiring
- stirring
- bath
- electrodeposition
- wiring board
- 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.)
- Expired
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- Insulated Metal Substrates For Printed Circuits (AREA)
Description
本発明は鋼板およびアルミニウム板等の導電性
基板を用いたプリント配線用基板に、優れた耐電
圧性、密着性等の物理的性質を有する平滑な絶縁
塗膜を与えるための塗装方法に関する。
近年電話交換機、民生用音響機器、コンピユー
ター機器、その他各種の配線を集約した機器の配
線回路を作成するに当り、それらの回路および基
板の寸法安定性、機械的強度、放熱性、経済性の
改良がますます望まれて来ている。
従来かかるプリント配線用基板として、ガラス
繊維強化エポキシ樹脂、あるいはフエノール樹脂
等の合成樹脂が使用されている。しかしこれら合
成樹脂基板は軽量ではあるが、寸法安定性、機械
的強度、放熱性等について充分満足できるもので
はなかつた。上記合成樹脂にかえて、鋼板および
アルミニウム板等の導電性基板を用いれば、かか
る欠点は克服されるが、これらは導電性であるた
めに、このままでプリント配線用に供し得ない。
導電性基板を絶縁性にするために絶縁塗料を塗布
することが考えられ、粉体塗料やあるいは粉体電
着塗料を塗布する方法〔特願昭53−100781号(特
開昭55−27647号、特公昭56−39076号)〕が提案
されているが、本発明はかかる方法の改良に係る
ものである。
通常、プリント配線用基板は直径2〜10mmの削
孔がある。かかる導電性プリント配線用基板を粉
体電着浴に浸漬した時に空気泡を抱き込むことが
多い。更に、基板素材には通常ロール目、ヤスリ
傷、その他物理的な傷が多くあり、これ等の部分
も、上記孔部と同様粉体電着浴に浸漬した時に、
局部的に粉体電着浴による濡れが悪くなり、空気
泡を抱き込むことになる。更にまた、基板への塗
膜の密着性の向上をはかるため、リン酸亜鉛ある
いはリン酸鉄等のリン酸塩化成処理などの適当な
前処理が施された場合、特にリン酸亜鉛処理が施
された場合、基板表面は微細な凹凸が多く、空気
泡を抱き込み易い。
このように空気泡を絶縁塗膜中に抱き込むと塗
膜の破壊電圧が低下し、絶縁性の低下となり所期
の目的を達せられなくなる問題が生じる。
本発明者は、上記の如き欠点を改良すべく鋭意
研究の結果、導電性プリント配線用基板をカチオ
ン粉体電着塗装法にて塗装するに際して、上記導
電性プリント配線用基板をカチオン粉体電着浴に
浸漬し、まず3〜30秒間は無通電の状態で、上記
導電性プリント配線用基板の表面での流速が10〜
80cm/秒となるように浴液を撹拌した後、上記流
速が5〜50cm/秒となるように浴液を撹拌しなが
ら通電してカチオン粉体電着塗装を行うと、空気
泡を塗膜中に抱き込むことなく、平滑で、絶縁性
にすぐれた塗膜を与えることを見出した。
本発明方法に用いるカチオン粉体電着塗装料は
顔料含有合成樹脂微粉体と水稀釈性カチオン性樹
脂を主成分としてなる。上記顔料含有合成樹脂微
粉体は熱硬化型エポキシ樹脂と当業界で一般に使
用される顔料、添加剤等を粉体塗料製造の常法に
より混練後微粉砕して得られる。その粒径は2〜
20μであることが望ましい。また絶縁の目的を損
わない限り、一部他の樹脂例えばポリエステル樹
脂、フエノール樹脂、エポキシウレタン樹脂、ウ
レタン樹脂、石油樹脂等を混入することもでき
る。
上記水稀釈性カチオン性樹脂は電着塗装実施
時、上記顔料含有合成樹脂微粉体に浴中での電気
泳動性を与える作用をする。かかる水稀釈性カチ
オン性樹脂はエポキシ樹脂を用いて作るのが好ま
しく、エポキシ樹脂に水稀釈性を与えるために1
級または2級アミンを付加し、更に酸性化合物で
中和する。
本発明方法を用いる電着浴は上記顔料含有合成
樹脂微粉体と水稀釈性カチオン性樹脂とを0.5〜
20:1の重量比で水中に分散または溶解して作
り、電着浴の固型分は5〜30重量%であることが
望ましい。
上記のようにして作成したカチオン粉体電着浴
に鋼板、アルミニウム板等の導電性プリント配線
用基板を浸漬する。本発明によれば浸漬後3〜30
秒間は無通電の状態で導電性プリント配線用基板
表面での流速が10〜80cm/秒、好ましくは30〜80
cm/秒となるように浴液を撹拌し、浸漬時基板表
面に抱き込んだ空気泡を除去する。この場合撹拌
流速が10cm/秒未満では抱き込んだ空気泡を除去
する効果が得られず、また80cm/秒を超える撹拌
流速では強すぎて、逆に電着浴中に空気泡を抱き
込み易くなる。また、該撹拌流速を与える時間は
3〜30秒間である。3秒間未満では空気泡除去の
効果が得られず、30秒間を超えて長時間の撹拌を
行つても、空気泡除去の効果の向上は見られず、
逆に水稀釈性カチオン性樹脂の水和に使用した酸
性化合物による腐食等の悪影響が顕れやすくな
る。一般に流速が大となればなる程時間は短くす
ることができる。
更に絶縁塗膜とプリント配線用基板との密着性
を向上させるために、プリント配線用基板をリン
酸亜鉛、リン酸鉄等の化成処理を行うことが多
い。かかる化成処理を行つた後、水洗水で濡れた
ままのプリント配線用基板を粉体電着浴に浸漬し
た場合、プリント配線用基板に近接した粉体電着
浴液が水で稀釈され濃度が低下する。この低濃度
の粉体電着浴下で電着塗装を行うと、水の電気分
解による水素ガス泡の大量発生があり、塗膜中に
水素ガスの抱き込みが起り易い。本発明方法によ
れば、水洗水による粉体電着浴の浴濃度の勾配を
解消し、低濃度での電着塗装が避けられる。
本発明方法は上記10〜80cm/秒の流速で浴液の
撹拌を3〜30秒間行つた後、5〜50cm/秒、好ま
しくは20〜30cm/秒の流速で浴液を撹拌しながら
通電を行い、粉体電着塗装をするものである。
即ち、前記空気泡の除去あるいは濃度勾配の解
消後被塗物を陰極とし、炭素、不銹鋼製等の不
蝕、不銹性の棒または板を対極の陽極とし、直流
電圧を印加する。この際、撹拌流速が弱いと、水
の電気分解により発生する水素ガスが絶縁塗膜中
に抱き込まれ易い、あるいは浴中に分散している
合成樹脂微粉体が沈降し易い等の欠点が生じる。
一方強すぎると被塗物が粉体電着浴中で安定に保
持されず、極間距離が一定に保たれず、均一な膜
厚が得られ難い。
撹拌を行うには、通常行われているノズルより
浴液を噴出させることで行つてもよいし、プロペ
ラを浴液中で回転させることで行つてもよい。ま
た、撹拌流の方向はプリント配線用基板の表面に
対して直角にするか平行にする。
塗装条件は浴液温度20〜30℃、電圧100〜
400V、通電時間5〜90秒、好ましくは浴液温度
20〜25℃、電圧150〜300V、通電時間10〜20秒で
ある。
電着された被塗物は、次いで常法により水洗、
水切乾燥工程を経て、焼付けし、電着被膜を硬化
させる。かくして3KV以上の耐電圧性を有する
平滑均一な絶縁被覆がプリント配線用導電性基板
上に形成できる。
本発明の方法を用いることによつて導電性プリ
ント配線用基板の有する多数の穿孔部および平面
に、その要求される厳密な寸法安定性を損うこと
なく、耐電圧性を有する均一膜厚の被膜を作るこ
とができる。
以下実施例を挙げて本発明を説明する。文中部
および%は全て重量部および重量%である。
粉体電着塗料の製造
(1) 粉体粒子の製造
エポキシ樹脂 エピコート1007(シエル化学)
40.0部
イソシアネート硬化剤 EH―118―2(旭電
化) 36.0
顔 料 チタンR―80(石原産業) 21.0
〃 カーボンMA―100(三菱化成) 0.5
〃 微粒シリカAEROSIL380(日本アエロシ
ル) 2.5
を通常の粉体塗料製造法によりエクストルーダ
ーで溶融混練りし、衝撃式粉砕機で10〜18μの
粒子径に粉砕した。
(2) 水稀釈性カチオン性樹脂の製造
エピコート1001(シエル化学) 488部
ジエタノールアミン 105
イソプロピルアルコール 250
を80℃で3時間還流下に反応させて液状の樹脂
を得た。
(3) 粉体電着塗料浴液の製造
上記カチオン性樹脂857部に氷酢酸38部およ
び脱イオン水5105部を加えて、デイゾルバーで
充分撹拌し、次いで上記粉体塗料5400部を加
え、高速回転ホモジナイザーで混合分散させた
後、固形分20%になるまで脱イオン水で稀釈
し、30000部の粉体電着塗料浴液を作成した。
実施例 1
電着槽にプロペラ撹拌機を設置し、被塗物とし
てのリン酸亜鉛処理した、多数の直径1〜5mmの
孔を有する鋼製のプリント配線用基板(250×200
×0.8mm)を浸漬し、無通電の状態で5秒間プリ
ント配線用基板の表面に平行で50cm/秒の流速と
なるよう撹拌後、撹拌流速を10cm/秒とし、下記
の条件で塗装した。対極として250×200mmのステ
ンレス板を被塗物の両側に浸漬した。
電着条件は次の如くであつた。
浴液温度 22℃
極間距離 15cm
極 比 /=1/1
電 圧 300V
通電時間 20秒
電着後、清水で水洗し、その後焼付を行つた。
焼付条件は80℃で10分、次いで80℃から200℃ま
で15分間で昇温し、200℃で15分焼付けた。得ら
れた塗膜の膜厚は135μで破壊耐電圧は4.5KVであ
つた。顕微鏡により、孔部断面の塗膜を検査した
ところ気泡は抱き込まれていなかつた。
実施例 2
実施例1において、プロペラ撹拌のかわりにノ
ズル噴流による撹拌を行つた。浸漬直後の無通電
状態での撹拌は、プリント配線用基板の表面に平
行で流速が80cm/秒で10秒間行い、電着塗装時の
撹拌は30cm/秒の流速で行つた。上記の条件以外
は実施例1と同様に塗装したところ得られた塗膜
厚は120μで破壊耐電圧は4.5KVであつた。顕微鏡
により孔部断面の塗膜を検査したところ気泡は抱
き込まれていなかつた。
比較例 1
実施例1において、浸漬直後直ちに通電し電着
塗装を行つた。電着塗装時の撹拌流速は20cm/秒
であつた。得られた塗膜厚は150μであつたが、
破壊耐電圧は0.8KVと低かつた。顕微鏡により孔
部断面の塗膜を検査したところ気泡が存在するこ
とが判つた。
比較例 2
実施例1において、浸漬直後の撹拌を行わず2
秒間静置後通電し電着塗装を行つた。電着塗装時
の撹拌流速は20cm/秒であつた。得られた塗膜厚
は140μであつたが、破壊耐電圧は0.7KVであつ
た。顕微鏡により孔部断面の塗膜を検査したとこ
ろ気泡が存在することが判つた。
以上の結果を第1表にまとめて示す。
The present invention relates to a coating method for providing a smooth insulating coating having excellent physical properties such as voltage resistance and adhesion to printed wiring boards using conductive substrates such as steel plates and aluminum plates. In recent years, when creating wiring circuits for telephone exchanges, consumer audio equipment, computer equipment, and other devices that integrate various types of wiring, improvements have been made in the dimensional stability, mechanical strength, heat dissipation, and economic efficiency of these circuits and boards. is becoming more and more desired. Conventionally, synthetic resins such as glass fiber-reinforced epoxy resins or phenolic resins have been used for such printed wiring boards. However, although these synthetic resin substrates are lightweight, they are not fully satisfactory in terms of dimensional stability, mechanical strength, heat dissipation, etc. If a conductive substrate such as a steel plate or an aluminum plate is used instead of the above-mentioned synthetic resin, this drawback can be overcome, but since these are conductive, they cannot be used as they are for printed wiring.
In order to make the conductive substrate insulating, it is possible to apply an insulating paint, and a method of applying powder paint or powder electrodeposition paint [Japanese Patent Application No. 53-100781 (Japanese Unexamined Patent Publication No. 55-27647) , Japanese Patent Publication No. 56-39076) has been proposed, and the present invention relates to an improvement of such a method. Usually, printed wiring boards have holes with a diameter of 2 to 10 mm. When such a conductive printed wiring board is immersed in a powder electrodeposition bath, air bubbles are often trapped. Furthermore, the substrate material usually has many roll marks, file scratches, and other physical scratches, and when immersed in the powder electrodeposition bath, these areas are also damaged, similar to the holes described above.
Wetting by the powder electrodeposition bath locally becomes poor and air bubbles are trapped. Furthermore, in order to improve the adhesion of the coating film to the substrate, a suitable pre-treatment such as a chemical phosphate treatment such as zinc phosphate or iron phosphate is applied, especially zinc phosphate treatment. In this case, the substrate surface has many fine irregularities and tends to trap air bubbles. If air bubbles are trapped in the insulating coating film in this way, the breakdown voltage of the coating film will be lowered, resulting in a decrease in insulation properties, causing the problem that the intended purpose cannot be achieved. As a result of intensive research in order to improve the above-mentioned drawbacks, the inventor of the present invention discovered that when coating a conductive printed wiring board using a cationic powder electrodeposition coating method, the conductive printed wiring board can be coated with a cationic powder electrodeposition coating method. Immerse the conductive printed wiring board in the bath, first without applying electricity for 3 to 30 seconds, until the flow velocity on the surface of the conductive printed wiring board is 10 to 10.
After stirring the bath liquid at a flow rate of 80 cm/sec, electricity is applied while stirring the bath liquid at a flow rate of 5 to 50 cm/sec to perform cationic powder electrodeposition coating, which removes air bubbles from the coating. It was discovered that a smooth coating film with excellent insulation properties can be provided without being trapped inside. The cationic powder electrodeposition coating material used in the method of the present invention is mainly composed of a pigment-containing synthetic resin fine powder and a water-dilutable cationic resin. The pigment-containing synthetic resin fine powder is obtained by kneading a thermosetting epoxy resin, pigments, additives, etc. commonly used in the art by a conventional method for producing powder coatings, and then finely pulverizing the resin. Its particle size is 2~
It is desirable that it be 20μ. Further, as long as the purpose of insulation is not impaired, other resins such as polyester resin, phenol resin, epoxy urethane resin, urethane resin, petroleum resin, etc. may be mixed in part. The water-dilutable cationic resin functions to impart electrophoretic properties to the pigment-containing synthetic resin fine powder in a bath during electrodeposition coating. Such a water-dilutable cationic resin is preferably made using an epoxy resin, and in order to impart water-dilubility to the epoxy resin, 1.
A primary or secondary amine is added and further neutralized with an acidic compound. The electrodeposition bath using the method of the present invention contains the pigment-containing synthetic resin fine powder and the water-dilutable cationic resin in an amount of 0.5 to
Preferably, the electrodeposition bath is prepared by dispersing or dissolving in water at a weight ratio of 20:1, and the solid content of the electrodeposition bath is 5 to 30% by weight. A conductive printed wiring board such as a steel plate or an aluminum plate is immersed in the cationic powder electrodeposition bath prepared as described above. According to the invention 3-30 minutes after soaking
The flow velocity on the surface of the conductive printed wiring board is 10 to 80 cm/sec, preferably 30 to 80 cm/sec, when no current is applied.
The bath solution is stirred at a rate of cm/second to remove air bubbles trapped on the substrate surface during immersion. In this case, if the stirring flow rate is less than 10 cm/sec, it will not be effective in removing trapped air bubbles, and if the stirring flow rate exceeds 80 cm/sec, it will be too strong and will conversely tend to trap air bubbles in the electrodeposition bath. Become. Further, the time period for applying the stirring flow rate is 3 to 30 seconds. If stirring is carried out for less than 3 seconds, the effect of removing air bubbles cannot be obtained, and even if stirring is performed for a long time exceeding 30 seconds, no improvement in the effect of removing air bubbles is observed.
Conversely, the acidic compound used to hydrate the water-dilutable cationic resin tends to cause adverse effects such as corrosion. Generally, the higher the flow rate, the shorter the time can be. Furthermore, in order to improve the adhesion between the insulating coating film and the printed wiring board, the printed wiring board is often subjected to chemical conversion treatment with zinc phosphate, iron phosphate, or the like. After such chemical conversion treatment, when a printed wiring board that is still wet with washing water is immersed in a powder electrodeposition bath, the powder electrodeposition bath liquid in the vicinity of the printed wiring board is diluted with water and its concentration is reduced. descend. When electrodeposition coating is performed in a powder electrodeposition bath with such a low concentration, a large amount of hydrogen gas bubbles are generated due to water electrolysis, and hydrogen gas is likely to be trapped in the coating film. According to the method of the present invention, the gradient in the bath concentration of the powder electrodeposition bath due to washing water is eliminated, and electrodeposition coating at low concentrations can be avoided. In the method of the present invention, after stirring the bath liquid for 3 to 30 seconds at a flow rate of 10 to 80 cm/sec, electricity is applied while stirring the bath liquid at a flow rate of 5 to 50 cm/sec, preferably 20 to 30 cm/sec. It is then coated with powder electrodeposition. That is, after the air bubbles have been removed or the concentration gradient has been resolved, a DC voltage is applied using the object to be coated as a cathode and a corrosion-resistant rod or plate made of carbon, stainless steel, etc. as a counter anode. At this time, if the stirring flow rate is low, there will be drawbacks such as hydrogen gas generated by water electrolysis being easily trapped in the insulating coating, or synthetic resin fine powder dispersed in the bath being likely to settle. .
On the other hand, if it is too strong, the object to be coated will not be stably held in the powder electrodeposition bath, the distance between the electrodes will not be kept constant, and it will be difficult to obtain a uniform film thickness. Stirring may be carried out by jetting out the bath liquid from a nozzle, as is commonly done, or by rotating a propeller in the bath liquid. Further, the direction of the stirring flow is perpendicular to or parallel to the surface of the printed wiring board. Painting conditions are bath liquid temperature 20~30℃, voltage 100~
400V, energizing time 5-90 seconds, preferably bath liquid temperature
The temperature is 20-25°C, the voltage is 150-300V, and the energization time is 10-20 seconds. The electrodeposited object is then washed with water in a conventional manner.
After a draining and drying process, it is baked to harden the electrodeposited film. In this way, a smooth and uniform insulating coating having a voltage resistance of 3 KV or more can be formed on a conductive substrate for printed wiring. By using the method of the present invention, a uniform film thickness with withstand voltage can be formed on the numerous perforations and flat surfaces of a conductive printed wiring board without compromising the required strict dimensional stability. A film can be created. The present invention will be explained below with reference to Examples. All parts and percentages are by weight. Manufacture of powder electrodeposition paint (1) Manufacture of powder particles Epoxy resin Epicoat 1007 (Ciel Chemical)
40.0 parts Isocyanate hardener EH-118-2 (Asahi Denka) 36.0 Pigment Titanium R-80 (Ishihara Sangyo) 21.0 Carbon MA-100 (Mitsubishi Kasei) 0.5 Fine silica AEROSIL 380 (Nippon Aerosil) 2.5 as normal powder The mixture was melted and kneaded using an extruder according to the paint manufacturing method, and then ground to a particle size of 10 to 18μ using an impact grinder. (2) Production of water-dilutable cationic resin Epicote 1001 (Siel Chemical) 488 parts diethanolamine 105 isopropyl alcohol 250 were reacted under reflux at 80°C for 3 hours to obtain a liquid resin. (3) Production of powder electrodeposition paint bath liquid Add 38 parts of glacial acetic acid and 5105 parts of deionized water to 857 parts of the above cationic resin, stir thoroughly with a dissolver, then add 5400 parts of the above powder paint, and add at high speed. After mixing and dispersing with a rotary homogenizer, the mixture was diluted with deionized water to a solid content of 20% to prepare 30,000 parts of a powder electrodeposition paint bath solution. Example 1 A propeller stirrer was installed in the electrodeposition bath, and a zinc phosphate-treated steel printed wiring board (250 x 200
x 0.8 mm) and stirred for 5 seconds in a non-energized state at a flow rate of 50 cm/sec parallel to the surface of the printed wiring board, then the stirring flow rate was set to 10 cm/sec, and coating was performed under the following conditions. As counter electrodes, stainless steel plates measuring 250 x 200 mm were immersed on both sides of the object to be coated. The electrodeposition conditions were as follows. Bath temperature: 22°C Distance between electrodes: 15cm Electrode ratio: /=1/1 Voltage: 300V Current application time: 20 seconds After electrodeposition, the electrodes were washed with clean water, and then baked.
The baking conditions were 80°C for 10 minutes, then the temperature was raised from 80°C to 200°C for 15 minutes, and baking was performed at 200°C for 15 minutes. The resulting coating film had a thickness of 135μ and a breakdown voltage of 4.5KV. When the coating film on the cross section of the hole was examined using a microscope, it was found that no air bubbles were trapped. Example 2 In Example 1, stirring by a nozzle jet was performed instead of propeller stirring. Immediately after dipping, stirring without electricity was performed for 10 seconds at a flow rate of 80 cm/sec parallel to the surface of the printed wiring board, and stirring during electrodeposition coating was performed at a flow rate of 30 cm/sec. Coating was carried out in the same manner as in Example 1 except for the above conditions, and the resulting coating film thickness was 120μ and breakdown voltage was 4.5KV. When the coating film on the cross section of the hole was examined using a microscope, it was found that no air bubbles were trapped. Comparative Example 1 In Example 1, electricity was applied immediately after dipping to perform electrodeposition coating. The stirring flow rate during electrodeposition coating was 20 cm/sec. The coating thickness obtained was 150μ,
The breakdown voltage was as low as 0.8KV. When the coating film on the cross section of the hole was examined using a microscope, it was found that air bubbles were present. Comparative Example 2 In Example 1, stirring was not performed immediately after immersion.
After standing still for a second, electricity was applied to perform electrodeposition coating. The stirring flow rate during electrodeposition coating was 20 cm/sec. The coating thickness obtained was 140μ, and the breakdown voltage was 0.7KV. When the coating film on the cross section of the hole was examined using a microscope, it was found that air bubbles were present. The above results are summarized in Table 1.
【表】
上記のように本発明方法によれば、塗膜中に抱
き込まれる気泡がなく、もしくはあつても非常に
少なく、膜厚が小さいにもかかわらず、破壊耐電
圧は4.5KVと充分実用に耐えるものとなつた。一
方、本発明方法によらない従来法では比較例に示
すように、塗膜中に気泡を多く抱き込み、またそ
の気泡も大きなものであつた。そのため破壊耐電
圧も0.8KV、0.7KVと低く実用にならなかつた。[Table] As described above, according to the method of the present invention, there are no or very few air bubbles trapped in the coating film, and despite the small film thickness, the breakdown voltage is sufficient at 4.5 KV. It has become practical. On the other hand, as shown in the comparative example, the conventional method, which does not rely on the method of the present invention, contained many air bubbles in the coating film, and the air bubbles were also large. As a result, the breakdown voltage was low, at 0.8KV and 0.7KV, making it impractical.
Claims (1)
オン粉体電着塗装法にて塗装するに際して、上記
導電性プリント配線用基板をカチオン粉体電着浴
に浸漬し、まず3〜30秒間は無通電の状態で上記
導電性プリント配線用基板の表面での流速が10〜
80cm/秒となるように浴液を撹拌した後、上記流
速が5〜50cm/秒となるように浴液を撹拌しなが
ら通電し、上記撹拌流を上記基板に対し平行また
は直角に流すことを特徴とする導電性プリント配
線用基板の塗装方法。1. When coating with a cationic powder electrodeposition coating method using a conductive printed wiring board as a cathode, the conductive printed wiring board is immersed in a cationic powder electrodeposition bath, and first no electricity is applied for 3 to 30 seconds. The flow velocity on the surface of the above conductive printed wiring board is 10~
After stirring the bath liquid so that the flow rate is 80 cm/sec, electricity is applied while stirring the bath liquid so that the flow rate is 5 to 50 cm/sec, and the stirring flow is caused to flow parallel or at right angles to the substrate. Features: A coating method for conductive printed wiring boards.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13730379A JPS5661198A (en) | 1979-10-24 | 1979-10-24 | Method of painting board for wiring conductive print |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13730379A JPS5661198A (en) | 1979-10-24 | 1979-10-24 | Method of painting board for wiring conductive print |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5661198A JPS5661198A (en) | 1981-05-26 |
| JPS6350880B2 true JPS6350880B2 (en) | 1988-10-12 |
Family
ID=15195526
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13730379A Granted JPS5661198A (en) | 1979-10-24 | 1979-10-24 | Method of painting board for wiring conductive print |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5661198A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04123261U (en) * | 1991-04-23 | 1992-11-06 | 株式会社アスカエンジニアリング | anode basket |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE785937A (en) * | 1971-07-08 | 1973-01-08 | Sandoz Sa | NEW DERIVATIVES OF QUINAZOLINE, THEIR PREPARATION AND THEIR APPLICATION AS MEDICINAL PRODUCTS |
| JPS5262661A (en) * | 1975-11-19 | 1977-05-24 | Nippon Telegraph & Telephone | Method of producing metallic core organic coating printed circuit wiring board |
-
1979
- 1979-10-24 JP JP13730379A patent/JPS5661198A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04123261U (en) * | 1991-04-23 | 1992-11-06 | 株式会社アスカエンジニアリング | anode basket |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5661198A (en) | 1981-05-26 |
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