JPS621245Y2 - - Google Patents
Info
- Publication number
- JPS621245Y2 JPS621245Y2 JP1981047112U JP4711281U JPS621245Y2 JP S621245 Y2 JPS621245 Y2 JP S621245Y2 JP 1981047112 U JP1981047112 U JP 1981047112U JP 4711281 U JP4711281 U JP 4711281U JP S621245 Y2 JPS621245 Y2 JP S621245Y2
- Authority
- JP
- Japan
- Prior art keywords
- electrodeposited
- water
- electrode
- electrodeposition
- conductor
- 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
Links
- 238000004070 electrodeposition Methods 0.000 claims description 18
- 239000004020 conductor Substances 0.000 claims description 10
- 239000003960 organic solvent Substances 0.000 claims description 10
- 239000002966 varnish Substances 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000011347 resin Substances 0.000 description 6
- 229920005989 resin Polymers 0.000 description 6
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 3
- 230000015556 catabolic process Effects 0.000 description 3
- 230000005684 electric field Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000004593 Epoxy Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
Landscapes
- Processes Specially Adapted For Manufacturing Cables (AREA)
Description
本考案は、絶縁電線を電着により連続製造する
ための連続電着装置に関する。
導体上に電着された直後の電着層は、析出樹脂
が石垣状に堆積した状態となつており、その状態
のまゝで焼付けたのではピンホールのある絶縁皮
膜しか得られないので、この問題を解決するため
に、焼付に先立つて電着層を予め有機溶媒にて処
理し、電着層中の樹脂を軽く溶解、膨潤等させて
互に融合し易い状態にもたらすことが行われてい
る。
ところで、電着ワニスとして、水分散ワニスを
用いたとき、電着層中には水分が残留している
が、本考案者らの研究によれば、水溶性又は部分
的に水溶性の有機溶媒にて処理するときの電着層
中に残留する水分量の多寡により処理効果が大き
く変る。即ち、残留水分量が過少であると有機溶
媒が電着層中に浸透し難く、而して電着層全体を
均一に処理し得ず、このため絶縁破壊強度の高い
焼付絶縁皮膜が形成され難い問題がある。また一
方、残留水分量が過大であると、焼付時の電着層
からの過度の水分蒸発のために電着絶縁皮膜に発
泡が生じ、やはり絶縁破壊強度が低下する。
引続く本考案者らの研究によれば、残留水分量
が析出樹脂量比にして約50〜80重量%程度である
とき良好な有機溶媒処理を行うことができ、ま
た、前記実用新案登録請求の範囲に示す本考案装
置を用いることにより電着直後の水分含有量を上
記範囲となし得、而して本考案の装置を用いるこ
とにより、絶縁破壊強度の優れた絶縁電線を電着
法により連続的に製造することができる。
付図は、本考案実施例の断面図であつて、1
は、水分散ワニス11が満たされ電着バスであ
り、その出口(水分散ワニスの水面)側には円筒
形の電極12が設置されている。
電極には、円筒形のほか、1枚又は平行2枚の
平板状、あるいはその他の形状のものであつても
よい。
電着バス1の入口から出口までの長さをLとし
たとき電極12の長さlは0.1L〜0.7Lである。L
は矢印の方向に下から上へ連続走行する被電着導
体Wの線速によつて多少異るが、線速は10〜50
m/分程度であり、その場合、Lは20〜200cm程
度が適当である。
2は直流電源であつて、該電源の1端は給電部
孔21を介して被電着導体Wに、一方他端は電極
12にそれぞれ接続されている。使用する水分散
ワニス11の種類により電極、被電着導体の課電
極性が決定される。電源2は、被電着導体Wと電
極との間に直流電圧を課電し得る直流電源であ
る。3は、電着バスの直上に設置された有機溶剤
処理装置、4は、更にその上に設置された焼付炉
である。
矢印の方向に連続走行する被電着導体Wは、電
着バス1中において電着される。電着層は、有機
溶剤処理装置3中において公知(たとえば特公昭
45−31555参照)の方法、条件にて高温度及び常
温の有機溶剤又はその蒸気あるいはミストにより
処理され、焼付炉4において公知の焼付温度にて
焼付けられる。
本考案の装置を用い、被電着導体Wと電極12
との間に直流電圧を課電して電着するときは、水
分散ワニスの種類を問はず電着層の含水率は、略
前記した値となるので直ちに装置3にて有機溶剤
処理を施されて良好な結果が得られる。これに対
して電極長が、上記した長さより長すぎても、短
かすぎても又電極を電着バスの入口や中央などに
設置しても電着層の含水率が前記範囲をはずれる
事になり、耐電圧特性の良好な絶縁電線は得られ
ない。
本考案においては、短尺の電極が電着バスの出
口側に設置されているため、被電着導体Wは入口
から出口に進むに従つて漸次強い電界に曝される
こととなるので、該導体上への電着は、入口近傍
では徐々に進み、出口に向う程急激となるが、こ
の電着の進行と同時に電界の作用による電着層の
引締め作用並びに該作用の結果としての適当の脱
水現象が生じて、上記した含水率の電着層が得ら
れる。
付表には各種実施例、比較例の装置を用いて絶
縁電線を製造した結果を示す。同表において電着
層含水率は、有機溶剤処理前の電着層の含水率を
示し、絶縁破壊強度及び外観は、焼付された電着
層についてのものである。電着層は、電着後直ち
にジメチルホルムアミド蒸気(温度約100℃)に
て約5秒間処理し、次いで最高温度400℃で焼付
けた。表示のワニスA,B,Cはそれぞれの組成
のものである。
又電線サイズは0.5mmφ皮膜厚0.025mm、線速20
m/minである。
ワニスA…エポキシーアクリル系エマルジヨン
樹脂分濃度約20%。
ワニスB…市販アクリルワニスCavalite
(Dupont社製)樹脂分濃度約20%。
ワニスC…市販アクリルワニスErcusol
(Bayer社製)樹脂分濃度約20%。
The present invention relates to a continuous electrodeposition apparatus for continuously manufacturing insulated wires by electrodeposition. Immediately after being electrodeposited on a conductor, the electrodeposited layer is in a state where the precipitated resin is deposited in a stone wall shape, and if it is baked in that state, only an insulating film with pinholes will be obtained. In order to solve this problem, the electrodeposited layer is treated with an organic solvent prior to baking to lightly dissolve and swell the resin in the electrodeposited layer, making it easier for them to fuse together. ing. By the way, when a water-dispersed varnish is used as an electrodeposited varnish, water remains in the electrodeposited layer, but according to research by the inventors, water-soluble or partially water-soluble organic solvents The treatment effect varies greatly depending on the amount of water remaining in the electrodeposited layer during treatment. That is, if the residual moisture content is too small, it is difficult for the organic solvent to penetrate into the electrodeposited layer, and the entire electrodeposited layer cannot be treated uniformly, resulting in the formation of a baked insulating film with high dielectric breakdown strength. There is a difficult problem. On the other hand, if the amount of residual moisture is excessive, foaming occurs in the electrodeposited insulating film due to excessive water evaporation from the electrodeposited layer during baking, which also reduces the dielectric breakdown strength. According to subsequent research by the inventors of the present invention, good organic solvent treatment can be performed when the residual water content is about 50 to 80% by weight relative to the amount of precipitated resin. By using the device of the present invention shown in the above range, the moisture content immediately after electrodeposition can be kept within the above range. Can be manufactured continuously. The attached figure is a sectional view of an embodiment of the present invention, and shows 1
is an electrodeposition bath filled with a water-dispersed varnish 11, and a cylindrical electrode 12 is installed on the outlet side (the water surface of the water-dispersed varnish). The electrode may have a cylindrical shape, one plate or two parallel plates, or other shapes. When L is the length from the entrance to the exit of the electrodeposition bath 1, the length l of the electrode 12 is 0.1L to 0.7L. L
varies somewhat depending on the linear speed of the electrodeposited conductor W that runs continuously from bottom to top in the direction of the arrow, but the linear speed is 10 to 50.
m/min, and in that case, L is suitably about 20 to 200 cm. Reference numeral 2 denotes a DC power source, one end of which is connected to the electrodeposited conductor W through a power supply hole 21, and the other end to the electrode 12. The polarity of the electrode and electrodeposited conductor is determined by the type of water-dispersed varnish 11 used. The power source 2 is a DC power source that can apply a DC voltage between the electrodeposited conductor W and the electrode. 3 is an organic solvent treatment device installed directly above the electrodeposition bath, and 4 is a baking furnace installed above it. The electrodeposited conductor W continuously traveling in the direction of the arrow is electrodeposited in the electrodeposition bus 1 . The electrodeposited layer is used in the organic solvent treatment apparatus 3 (for example, in the
45-31555) using an organic solvent or its vapor or mist at high temperature and room temperature, and baked in a baking furnace 4 at a known baking temperature. Using the device of the present invention, the electrodeposited conductor W and the electrode 12
When electrodepositing by applying a direct voltage between good results are obtained. On the other hand, if the electrode length is longer or shorter than the above-mentioned length, or if the electrode is installed at the entrance or center of the electrodeposition bath, the moisture content of the electrodeposition layer may fall outside the above range. Therefore, an insulated wire with good voltage resistance characteristics cannot be obtained. In the present invention, since a short electrode is installed on the exit side of the electrodeposition bath, the electrodeposited conductor W is exposed to a gradually stronger electric field as it progresses from the entrance to the exit. The upward electrodeposition progresses gradually near the entrance and becomes more rapid toward the exit.At the same time as this electrodeposition progresses, the action of the electric field tightens the electrodeposited layer, and as a result of this action, appropriate dehydration occurs. The phenomenon occurs and an electrodeposited layer having the moisture content described above is obtained. The attached table shows the results of manufacturing insulated wires using the devices of various examples and comparative examples. In the same table, the water content of the electrodeposited layer indicates the water content of the electrodeposition layer before organic solvent treatment, and the dielectric breakdown strength and appearance are for the baked electrodeposition layer. Immediately after electrodeposition, the electrodeposited layer was treated with dimethylformamide vapor (temperature of about 100°C) for about 5 seconds, and then baked at a maximum temperature of 400°C. Varnishes A, B, and C shown are of respective compositions. Also, the wire size is 0.5mmφ, the coating thickness is 0.025mm, and the wire speed is 20.
m/min. Varnish A: Epoxy acrylic emulsion resin concentration approximately 20%. Varnish B...Commercially available acrylic varnish Cavalite
(Manufactured by Dupont) Resin concentration approximately 20%. Varnish C…Commercial acrylic varnish Ercusol
(Manufactured by Bayer) Resin concentration approximately 20%.
【表】【table】
付図は、本考案実施例の断面図であつて、1は
電着バス、12は電着バスの出口に設置された電
極、2は電源、3は有機溶剤処理装置、4は焼付
炉。
The attached figure is a sectional view of an embodiment of the present invention, in which 1 is an electrodeposition bath, 12 is an electrode installed at the outlet of the electrodeposition bath, 2 is a power source, 3 is an organic solvent treatment device, and 4 is a baking furnace.
Claims (1)
出口に近接して設置された長さ0.1L〜0.7L(Lは
電着バスの入口及び出口の間の長さ)の電極と、
被電着導体と該電極との間に直流電圧を課電し得
る課電装置、並びに導体上に電着された電着層を
水溶性又は部分的に水溶性の有機溶剤で処理する
装置とからなることを特徴とする連続電着装置。 an electrodeposited bath filled with a water-dispersed varnish; an electrode with a length of 0.1L to 0.7L (L is the length between the inlet and the outlet of the electrocoat bath) installed close to the outlet of the bath;
A charging device capable of applying a DC voltage between an electrodeposited conductor and the electrode, and a device that treats an electrodeposited layer electrodeposited on a conductor with a water-soluble or partially water-soluble organic solvent. A continuous electrodeposition device comprising:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1981047112U JPS621245Y2 (en) | 1981-03-31 | 1981-03-31 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1981047112U JPS621245Y2 (en) | 1981-03-31 | 1981-03-31 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS57158772U JPS57158772U (en) | 1982-10-05 |
JPS621245Y2 true JPS621245Y2 (en) | 1987-01-13 |
Family
ID=29843932
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1981047112U Expired JPS621245Y2 (en) | 1981-03-31 | 1981-03-31 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS621245Y2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1623438A4 (en) * | 2003-05-12 | 2008-07-09 | Nippon Paint Co Ltd | Method of coating a square wire and an insulated wire of a square wire |
JP5377535B2 (en) * | 2011-01-31 | 2013-12-25 | 三菱電線工業株式会社 | Insulated wire manufacturing method and manufacturing apparatus |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49129732A (en) * | 1973-04-14 | 1974-12-12 |
-
1981
- 1981-03-31 JP JP1981047112U patent/JPS621245Y2/ja not_active Expired
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49129732A (en) * | 1973-04-14 | 1974-12-12 |
Also Published As
Publication number | Publication date |
---|---|
JPS57158772U (en) | 1982-10-05 |
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