JPS6129729Y2 - - Google Patents

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Publication number
JPS6129729Y2
JPS6129729Y2 JP4711381U JP4711381U JPS6129729Y2 JP S6129729 Y2 JPS6129729 Y2 JP S6129729Y2 JP 4711381 U JP4711381 U JP 4711381U JP 4711381 U JP4711381 U JP 4711381U JP S6129729 Y2 JPS6129729 Y2 JP S6129729Y2
Authority
JP
Japan
Prior art keywords
electrodeposited
electrode
electrodeposition
water
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
Application number
JP4711381U
Other languages
Japanese (ja)
Other versions
JPS57158773U (en
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 filed Critical
Priority to JP4711381U priority Critical patent/JPS6129729Y2/ja
Publication of JPS57158773U publication Critical patent/JPS57158773U/ja
Application granted granted Critical
Publication of JPS6129729Y2 publication Critical patent/JPS6129729Y2/ja
Expired legal-status Critical Current

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Description

【考案の詳細な説明】[Detailed explanation of the idea]

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、折出樹脂
が石垣状に推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高温度の水又は
水蒸気にて処理し、電着層中の樹脂同志を強く凝
集させて連続性のある皮膜に改質することが行わ
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、電着層中には多量の水分が残留して
いるが、本考案者らの研究によれば、高温度の水
又は水蒸気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水処理を行う前に
電着層に亀裂が生じる問題がある。また一方、残
留水分量が過大であると、高温度の水又は水蒸気
処理時及び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絶縁破壊強度
の良好な皮膜が得られない。 引続く本考案者らの研究によれば、残留水分量
が折出樹脂量比にして約30〜60重量%程度である
とき良好な水処理が行うことができ、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
ることにより発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
水媒体ワニス11が満された電着バスでありその
出口(水媒体ワニスの水面)側には円筒形又はリ
ング状の電極に12が設置されている。 電極には、円筒形などのほか、1枚又は平行2
枚の平板電極あるいはその他の形状のものでもよ
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0.005L〜0.3L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の線速によつて異るが、線速は10〜
50m/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端は供電部
材21を介して被電着導体Wに一方他端は電極1
2にそれぞれ接続されている。使用する水媒体ワ
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水処理装置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。電着層は水処理
装置3中において公知(たとえば特開昭52−
138689参照)の方法、条件にて高温度の水又は水
蒸気により処理され、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
媒体ワニスの種類と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にて水処理を
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、また電極を電着バスの入口
や中央などに設置したりしても電着層の含水率が
前記した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
着層含水率は水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、電着後温度400℃
の水蒸気にて約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はそれぞれ次の組成の
ものである。又電線サイズは0.5mmφ、皮膜厚
0.025mm線速20m/minである。 ワニスA……エポキシ−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
(Dupon′t社製)樹脂分濃度約20%に希
釈して使用。 ワニスC……市販アクリルワニスErcusol
(Bayer社製)樹脂分濃度約20%に希釈
して使用。
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 deposited 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. Therefore, in order to solve this problem, the electrodeposition layer is treated with high-temperature water or steam prior to baking, and the resin in the electrodeposition layer is strongly coagulated to form a continuous film. things are being done. By the way, when a water-dispersed varnish is used as an electrodeposited varnish, a large amount of water remains in the electrodeposited layer, but according to research by the present inventors, it is possible to treat it with high-temperature water or steam. The treatment effect varies greatly depending on the amount of water remaining in the electrodeposited layer. That is, if the residual moisture content is too small, there is a problem that cracks may occur in the electrodeposited layer before water treatment is performed. On the other hand, if the residual moisture content is excessive, foaming may occur in the electrodeposited insulating film due to excessive moisture evaporation from the electrodeposited layer during high-temperature water or steam treatment and during baking, resulting in poor dielectric breakdown strength. A film cannot be obtained. According to subsequent research by the inventors of the present invention, good water treatment can be performed when the residual water content is about 30 to 60% 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 departure and landing can be kept within the above range, and by using the device of the present invention, insulated wires with excellent dielectric breakdown strength can be continuously produced by electrodeposition. can be manufactured. The attached figure is a sectional view of an embodiment of the present invention, in which 1 is an electrodeposition bath filled with aqueous varnish 11, and a cylindrical or ring-shaped electrode 12 is provided on the outlet side (water surface of the aqueous varnish). is installed. In addition to cylindrical shapes, electrodes may have one or two parallel electrodes.
It may be a flat plate electrode or one of 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 0.005L to 0.3L. L varies depending on the linear speed of the electrodeposited conductor W that continuously runs from bottom to top in the direction of the arrow, but the linear speed is 10~
The speed is about 50 m/min, and in that case, L is suitably about 20 to 200 cm. 2 is a DC power source, one end of which is connected to the electrodeposited conductor W via a power supply member 21, and the other end is connected to the electrode 1.
2 are connected to each other. The polarity of the electrode and electrodeposited conductor is determined by the type of aqueous 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 a water treatment device 4 installed directly above the electrodeposited bath.
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 known in the water treatment equipment 3 (for example, in Japanese Patent Application Laid-Open No.
138689) using high-temperature water or steam, 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 DC voltage between the varnish and the varnish, the water content of the electrodeposited layer will be approximately the above value regardless of the type of aqueous varnish, so immediately water treatment is performed in the device 3. Good results can be obtained. On the other hand, even if the electrode length is longer or shorter than the above-mentioned length, or even if the electrode is installed at the entrance or center of the electrodeposition bath, the moisture content of the electrodeposition layer will remain within the above-mentioned range. As a result, 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, but at the same time as this electrodeposition progresses, the action of the electric field tightens the electrodeposited layer and the dehydration phenomenon occurs as a result of this action. As a result, 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 electrodeposition layer indicates the water content of the electrodeposition layer before water treatment.
Breakdown strength and appearance are for baked electrodeposited layers. The temperature of the electrodeposited layer is 400℃ after electrodeposition.
water vapor for about 5 seconds, then heat to the highest temperature.
Baked at 400℃. Varnishes A, B, and C shown have the following compositions. Also, the wire size is 0.5mmφ, and the coating thickness is
The linear velocity is 0.025mm and 20m/min. Varnish A: Epoxy-acrylic emulsion resin concentration approximately 20% Varnish B: Commercially available acrylic varnish, Cavalite
(Manufactured by Dupon't) Used after diluting the resin concentration to approximately 20%. Varnish C...Commercially available acrylic varnish Ercusol
(Manufactured by Bayer) Diluted to a resin concentration of approximately 20%.

【表】【table】

【表】【table】 【図面の簡単な説明】[Brief explanation of drawings]

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は電線、3は高温水又は水蒸気処理装置、
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 an electric wire, 3 is a high-temperature water or steam treatment device,
4 is a baking furnace.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 水分散ワニスを満した電着バスと、上記バス出
口に近接して設置された長さ0.005L〜0.3L(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
高温度の水又は水蒸気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 water-dispersed varnish; an electrode with a length of 0.005L to 0.3L (L is the length between the inlet and the outlet of the electrocoat bath) installed close to the outlet of the bath;
It is characterized by comprising a voltage applying device capable of applying a DC voltage between the electrodeposited conductor and the electrode, and a device that treats the electrodeposited layer on the conductor with high-temperature water or steam. Continuous electrodeposition equipment.
JP4711381U 1981-03-31 1981-03-31 Expired JPS6129729Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4711381U JPS6129729Y2 (en) 1981-03-31 1981-03-31

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4711381U JPS6129729Y2 (en) 1981-03-31 1981-03-31

Publications (2)

Publication Number Publication Date
JPS57158773U JPS57158773U (en) 1982-10-05
JPS6129729Y2 true JPS6129729Y2 (en) 1986-09-01

Family

ID=29843933

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4711381U Expired JPS6129729Y2 (en) 1981-03-31 1981-03-31

Country Status (1)

Country Link
JP (1) JPS6129729Y2 (en)

Also Published As

Publication number Publication date
JPS57158773U (en) 1982-10-05

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