JPS5919613B2 - Method for manufacturing enamel insulated wire and equipment for manufacturing the same - Google Patents
Method for manufacturing enamel insulated wire and equipment for manufacturing the sameInfo
- Publication number
- JPS5919613B2 JPS5919613B2 JP1765181A JP1765181A JPS5919613B2 JP S5919613 B2 JPS5919613 B2 JP S5919613B2 JP 1765181 A JP1765181 A JP 1765181A JP 1765181 A JP1765181 A JP 1765181A JP S5919613 B2 JPS5919613 B2 JP S5919613B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- air
- baking
- baking furnace
- combustion
- 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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- Application Of Or Painting With Fluid Materials (AREA)
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Description
【発明の詳細な説明】
本発明は、エナメル絶縁電線の製造方法及び製造装置、
特に、竪形焼付炉を有する装置の改良に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a method and apparatus for manufacturing an enamel insulated wire,
In particular, the present invention relates to improvements in equipment having a vertical baking furnace.
エナメル絶縁電線は、通常焼鈍された銅線あるいはアル
ミニウム線を、竪形エナメル焼付装置によつてエナメル
を塗布、焼付けして製造している。Enamel insulated wires are usually manufactured by applying enamel to an annealed copper wire or aluminum wire using a vertical enamel baking device and baking the wire.
前記竪形エナメル焼付装置は、第1図に示す如くヒータ
ー2を内蔵する焼付炉1の下端に下部開口3を、上端に
上部開口10を設け、下端開口3には調節用ノブ5によ
つて開閉する空気遮弊板4a34bを設け、その下にダ
イスホルダー7によつて保持したダイス6、塗料槽8及
びターンシーブ9を順次設け、焼鈍炉(図示せず)によ
つて焼鈍した軟銅線あるいは軟アルミニウム線W(以下
、素線という)を、ターンシーブ9を介して塗料槽8に
通してその表面に塗料を塗布し、これを次にダイス6に
よつて均一、一定量の塗布量に調整した後、下部開口3
から焼付炉1内に通し焼付け、それを上部開口10より
冷却室11を通して冷却しターンシーブ12を介して引
き出す構造で、普通、この操作を6〜8回繰り返して製
造するが、経済性を考えて10〜30本同時に同じ焼付
炉で製造し、1炉2サイズを左右に掛合せるのが一般的
である。この製造過程では、素線Wに塗布されたエナメ
ル塗料がヒーター2によつて加熱され溶剤分の蒸発、塗
膜の硬化がなされる際に溶剤ガスが発生するから、前記
焼付炉1には燃焼室13を設け、該燃焼室13にはプレ
ヒータ一14及び触媒15を設け、前記ガスは前記プレ
ヒータ一141こよつて必要に応じて加熱した後、前記
触媒15によつて反応燃焼させ、ブロワ−16によつて
一部を大気に放出し一部を炉1内に循環させて焼付けの
加熱に再利用する構造となつている。As shown in FIG. 1, the vertical enamel baking apparatus has a lower opening 3 at the lower end of a baking furnace 1 having a built-in heater 2, and an upper opening 10 at the upper end. An air shielding plate 4a34b that opens and closes is provided, and a die 6 held by a die holder 7, a paint tank 8, and a turn sheave 9 are sequentially provided thereunder. The aluminum wire W (hereinafter referred to as wire) was passed through a turn sieve 9 into a paint tank 8 to coat its surface with paint, and then the die 6 was used to adjust the coating amount to a uniform and constant amount. Back, lower opening 3
It has a structure in which it is baked through a baking furnace 1, cooled through an upper opening 10 through a cooling chamber 11, and pulled out through a turn sheave 12. Normally, this operation is repeated 6 to 8 times, but in consideration of economic efficiency. It is common to manufacture 10 to 30 pieces at the same time in the same baking furnace, with two sizes of one furnace stacked on the left and right. In this manufacturing process, solvent gas is generated when the enamel paint applied to the wire W is heated by the heater 2 to evaporate the solvent and harden the paint film. A chamber 13 is provided, and the combustion chamber 13 is provided with a preheater 14 and a catalyst 15, and the gas is heated as necessary by the preheater 141, and then reacted and combusted by the catalyst 15. The structure is such that a portion is released into the atmosphere and a portion is circulated within the furnace 1 and reused for heating for baking.
また、焼付炉1は堅形炉kよる煙突効果で上昇気流が生
ずるため、上部開口10の出口には間隙17を設け、そ
の間隙17に外部より高速の新しい空気を吹き込みこれ
を防止する構造いわゆるエアカーテン装置が設けられて
いる。尚、18はエアカーテン装置の排気通路である。In addition, since the baking furnace 1 generates an upward air current due to the chimney effect of the vertical furnace k, a gap 17 is provided at the outlet of the upper opening 10, and new air at high speed is blown from the outside into the gap 17 to prevent this so-called structure. An air curtain device is provided. Note that 18 is an exhaust passage of the air curtain device.
そして、前記堅形エナメル焼付炉1の有効炉長は、炉の
タイプによつてそれぞれ相違があるが、通常5〜8mが
標準で、その焼付温度はエナメル塗料の種類、焼付条件
によつて異なるが炉上部400〜500℃、炉中部35
0〜450℃、炉下部200〜350℃の範囲で設定す
るが通常である。以上は従来の代表的な焼付装置の構造
について説明したもので、この他に溶剤ガスの触媒、燃
焼系統に種々の工夫を加えたものが考えられているしか
し、前記の如く従来の堅形エナメル焼付装置1こは、次
のような欠点がある。The effective length of the rigid enamel baking furnace 1 varies depending on the type of furnace, but the standard is usually 5 to 8 m, and the baking temperature varies depending on the type of enamel paint and baking conditions. The upper part of the furnace is 400-500℃, the middle part of the furnace is 35℃.
It is normal to set the temperature in the range of 0 to 450°C and 200 to 350°C in the lower part of the furnace. The above is an explanation of the structure of a typical conventional printing device.In addition to this, devices with various improvements to the solvent gas catalyst and combustion system are being considered.However, as mentioned above, conventional hard enamel printing devices The printing device 1 has the following drawbacks.
まず、焼付炉1に入る空気量が過剰になることである。First, the amount of air entering the baking furnace 1 becomes excessive.
炉1に空気を入れる必要性は、エナメル絶縁電線の製造
中に炉1内で定常的に発生するエナメル塗料溶剤ガスを
触媒によつて燃焼するためである。従つて、この空気量
は、溶剤ガスを完全燃焼するに必要な空気量を炉1内に
導入してやればよい)のであつて、これより過剰の場合
は、その分だけエネルギー損失となるし、過小の場合は
不完全燃焼というトラブルを生ずる。It is necessary to introduce air into the furnace 1 because the enamel paint solvent gas that is constantly generated in the furnace 1 during the manufacture of enamel insulated wires is combusted by a catalyst. Therefore, it is sufficient to introduce the amount of air necessary to completely burn the solvent gas into the furnace 1. In this case, the problem of incomplete combustion occurs.
例えば、この必要空気量を、今、線径0.9鱈のJIS
l種ポリエステルイミド線を堅形エナメル焼付炉で16
本掛、炉温を上部450℃、中部350℃、下部300
℃に設定し、焼付線速20m/分でポリエステルイミド
塗料(樹脂分33%、メタクレゾール60%、石油ナフ
サ7%)を用いて製造するとすると、溶剤が炉内で蒸発
し完全燃焼する必要な空気量は、空気比1.2とすると
20℃換算で約8901/分となる。For example, this required air amount is now JIS for wire diameter 0.9 cod.
Type L polyester imide wire is heated in a rigid enamel baking furnace.
Honkake, set the furnace temperature to 450℃ in the upper part, 350℃ in the middle, and 300℃ in the lower part.
℃, and a baking line speed of 20 m/min is used to manufacture polyester imide paint (resin content: 33%, meta-cresol: 60%, petroleum naphtha: 7%). If the air ratio is 1.2, the air volume is approximately 8901/min at 20°C.
しかしながら第1図に示したような空気遮弊板4a,4
bの間隙は、走行する素線Wがその空気遮弊板4a,4
bと接触することを防ぐ必要上、その間隔は15〜20
11程度とならざるを得ず、堅形炉による煙突効果と炉
内循環気流とによりこの必要空気量は5〜7倍の空気が
過剰に吸人されているのが実情である。また、焼付炉1
の上部開口10においては、炉1内からの上昇気流を防
ぐために間隙17から外部より高速の気流を吹き込んで
防止するいわゆるエアカーテン構造となつているが、炉
1の巾方向にこの上昇気流を均一に押えることができず
、この部分で高温の炉内ガスと外部のエアカーテンの冷
たい空気が接触するため排ガスに含有する未燃焼分の溶
剤、短分子の樹脂が、時間の経過により凝縮し、そのま
ま放置しておくと製品に重大な悪影響をもたらすので短
期間に炉1を止めて清掃保守しなければならないという
欠点もある。However, the air shielding plates 4a, 4 as shown in FIG.
The air shielding plates 4a, 4 are separated by the gap b between the running strands W.
Due to the need to prevent contact with b, the interval is 15 to 20
The actual situation is that due to the chimney effect of the vertical furnace and the circulating air in the furnace, an excessive amount of air is drawn in, which is 5 to 7 times the required air amount. In addition, baking furnace 1
The upper opening 10 has a so-called air curtain structure in which high-speed airflow is blown from the outside through a gap 17 to prevent rising airflow from inside the furnace 1. Because the hot gas inside the furnace comes into contact with the cold air from the air curtain outside, the unburned solvent and short-molecule resin contained in the exhaust gas condense over time. However, if left as is, it will have a serious adverse effect on the product, so there is also the drawback that the furnace 1 must be shut down for a short period of time for cleaning and maintenance.
更に、焼付炉1の構造として触媒燃焼後の排ガス熱を炉
1内に循環させ再利用する構造のため並列する焼付炉の
片側をサイズ交換などで休転した場合、排ガスの燃焼が
とまると、瞬間的にヒーター2で補ぎない切れない微妙
な温度変化が生じ、もう片側で製造中の製品に重大な影
響を与える。Furthermore, since the structure of the baking furnace 1 is such that exhaust gas heat after catalytic combustion is circulated and reused within the furnace 1, if one side of the parallel baking furnaces is shut down due to a size change, etc., once the combustion of the exhaust gas has stopped, A subtle temperature change occurs instantaneously that cannot be compensated for by heater 2, which seriously affects the product being manufactured on the other side.
この現象は、休転していて運転を再開した場合も同様に
みられることである。この原因は焼付炉が左右一体とな
つて構造的に個別に独立しておらず、ヒーター2も一体
であり、温度制御系統、循環系統及びブロワ一を一括し
た構造としているためであると考えられる。This phenomenon also occurs when the engine is restarted after being inactive. This is thought to be due to the fact that the left and right baking furnaces are integrated, so they are not structurally independent, and the heater 2 is also integrated, making the temperature control system, circulation system, and blower all integrated. .
本発明は、このような点に鑑み前記欠点を解決したエナ
メル絶縁電線の製造方法及びその装置を提供せんとする
もので、その要旨は、塗料槽を通して導体上にエナメル
塗料を塗布し、ダイスを通して導体上のエナメル塗料層
を所定の厚さに均層化し、高温の焼付炉を通してエナメ
ル塗料層の溶剤を揮散、離脱させて導体上にエナメル塗
料を焼付けた後、冷却器を通して冷却固化するエナメル
絶縁電線の製造方法において、前記揮散、離脱させた溶
剤蒸気に空気を混合し、これを燃焼して高温ガスを作り
、この高温ガスを前記溶剤蒸気混合用空気の加熱に使用
した後、その一部を前記焼付炉の加熱に使用し、残部を
系外へ排出するとともに、他方前記高温ガスにより加熱
された空気は前記溶剤の燃焼に使用するに先立ち前記焼
付炉の出口に設けられたエアカーテン装置のエアとして
使用するエナメル絶縁電線の製造方法の第1の発明と、
下端に下部開口を、上端に上部開口を有する堅形焼付炉
の下方にダイス及び塗料槽を配し、上部開口近傍にエア
カーテン装置を設けてなるエナメル絶縁電線の製造装置
において、前記焼付炉の下部開口に密閉室を設けるとと
もに、別途燃焼炉と熱交換器とを新設し、熱交換器には
空気入口を連結し、前記熱交換器とエアカーテン装置と
の間、前記焼付炉の上部と前記燃焼炉との間、前記燃焼
炉と前記熱交換器との間及び前記交換器と前記焼付炉の
下部あるいは前記密閉室との間にそれぞれ通気路を設け
てなるエナメル絶縁電線の製造装置の第2の発明とに係
るものである。In view of these points, it is an object of the present invention to provide a method and apparatus for manufacturing an enamel insulated wire that solves the above-mentioned drawbacks. Enamel insulation involves uniformizing the enamel paint layer on the conductor to a predetermined thickness, volatilizing and separating the solvent in the enamel paint layer through a high-temperature baking furnace, and baking the enamel paint onto the conductor, which is then cooled and solidified through a cooler. In the method for manufacturing electric wires, air is mixed with the volatilized and separated solvent vapor, the mixture is combusted to produce high-temperature gas, and after this high-temperature gas is used to heat the solvent vapor mixing air, a part of it is is used to heat the baking furnace, and the remainder is discharged to the outside of the system, while the air heated by the high-temperature gas is heated by an air curtain device installed at the outlet of the baking furnace before being used for combustion of the solvent. A first invention of a method for manufacturing an enamel insulated wire used as air;
In an apparatus for manufacturing enameled insulated wire, the baking furnace has a lower opening at the lower end and an upper opening at the upper end. In addition to providing a sealed chamber in the lower opening, a combustion furnace and a heat exchanger are newly installed, an air inlet is connected to the heat exchanger, and a space between the heat exchanger and the air curtain device and the upper part of the baking furnace is installed. An apparatus for manufacturing an enameled insulated wire, comprising a ventilation passage between the combustion furnace, between the combustion furnace and the heat exchanger, and between the exchanger and the lower part of the baking furnace or the sealed chamber. This relates to the second invention.
以下、第2図乃至第4図について本発明の実施例を説明
する。Embodiments of the present invention will be described below with reference to FIGS. 2 to 4.
第2図において、20はヒーター21を内蔵し下端に下
部開口22を、上端に上部開口23を有する堅形焼付炉
で、下部開口22は、例えば蝶番25にて開閉自在の密
閉室24を設け密閉する。In FIG. 2, reference numeral 20 denotes a vertical baking furnace that includes a built-in heater 21 and has a lower opening 22 at the lower end and an upper opening 23 at the upper end. Seal tightly.
この密閉室24を開閉自在の構造とするのは線掛け作業
が行えるようにするためである。前記密閉室24にはそ
の下端に素線Wが通る通過孔26を設け、この通過孔2
6には隣設して取り外し可能にダイスホルダー28を設
けこれにダイス27を取り付けその下方にはエナメル塗
料槽29を設ける。The closed chamber 24 is designed to be able to be opened and closed in order to enable line hanging work. The sealed chamber 24 is provided at its lower end with a passage hole 26 through which the wire W passes, and this passage hole 2
A removable die holder 28 is provided adjacent to 6 and a die 27 is attached thereto, and an enamel paint tank 29 is provided below it.
この塗料槽29は前記ダイスホルダー28と一体に設け
ることもできる。30は触媒32を備えた燃焼炉で、該
燃焼炉30の一端は前記焼付炉20の先端部と連通され
、また、燃焼炉30の他端は熱交換器37の一端と連通
する。This paint tank 29 can also be provided integrally with the die holder 28. Reference numeral 30 denotes a combustion furnace equipped with a catalyst 32. One end of the combustion furnace 30 communicates with the tip of the baking furnace 20, and the other end of the combustion furnace 30 communicates with one end of a heat exchanger 37.
また、熱交換器37の他端と焼付炉20の下端部とを通
気路33で連通する。Further, the other end of the heat exchanger 37 and the lower end of the baking furnace 20 are communicated through a ventilation passage 33.
熱交換器37には、外部からの新鮮空気の取入れ口34
aと加熱空気出口34bが付いていて、この熱交換器3
7の加熱空気出口34bは前記焼付炉20の上部開口2
3近傍のエアカーテン装置35に連結する。36は燃焼
炉30に内蔵されたプロア一(可変速モータ付)で、エ
アカーテン装置35に吹き込まれた空気と炉20内で発
生した溶剤蒸気とを燃焼炉30内に吸い込むとともに、
炉30内で溶剤蒸気を燃焼させることにより生じた高温
ガスを熱交換器37及び通気路33を径由して焼付炉2
0の中下部、下端部或は密閉室24から焼付炉20内に
循環させるものである。The heat exchanger 37 has a fresh air intake port 34 from the outside.
a and a heated air outlet 34b, and this heat exchanger 3
The heated air outlet 34b of No. 7 is connected to the upper opening 2 of the baking furnace 20.
3 is connected to the nearby air curtain device 35. 36 is a blower (equipped with a variable speed motor) built into the combustion furnace 30, which sucks the air blown into the air curtain device 35 and the solvent vapor generated in the furnace 20 into the combustion furnace 30, and
The high-temperature gas generated by burning the solvent vapor in the furnace 30 is passed through the heat exchanger 37 and the ventilation passage 33 to the baking furnace 2.
0 or the sealed chamber 24 into the baking furnace 20.
また、前記加熱空気の通路34bは、熱交換器37によ
り高温ガスを加熱媒体として加熱した空気をエアーカー
テン装置35に送り込むのに使われる。更に、前記通気
路33にはダンパー38及び流量計39を設け、炉20
内への高温ガスの流入量を可変速プロアモータ(36.
M)で調節するようにすると有効である。Further, the heated air passage 34b is used to send air heated by the heat exchanger 37 using high temperature gas as a heating medium to the air curtain device 35. Furthermore, a damper 38 and a flow meter 39 are provided in the ventilation passage 33, and the furnace 20
A variable speed propeller motor (36.
It is effective to adjust it with M).
尚、40は余剰の高温ガスの排出通路、41は冷却室、
42,43はターンシーブである。In addition, 40 is a discharge passage for excess high temperature gas, 41 is a cooling chamber,
42 and 43 are turn sheaves.
しかして、素線Wを、ターンシーブ42を介して塗料槽
29に通してその表面に塗料を塗布し、これを次にダイ
ス27によつて均厚層に調整した後、通過孔26より密
閉室24を通し更に下部開口22から焼付炉20内に通
し焼付けし、それを冷却室41を通して冷却固化しター
ンシーブ43を介して引き出しエナメル絶縁電線を製造
するものであるが、焼付炉20の下部開口22は密閉室
24で密閉され外気を遮断しているうで、焼付炉20内
には、通路34aより吹き込まれた熱交換器37で加熱
された高温の空気と炉20内で発生した溶剤蒸気の混合
ガスとが燃焼炉30で製造された高温ガスだけが循環す
ることになる。従つて、焼付炉20内への空気は、必要
最少量8901/分だけ熱交換した高温の空気を通路3
4aより導入すればよく、排気も最少必要空気量890
1/分に見合う量(450℃で23001/分)だけ排
気通路40より排出すればよいから、炉1内の熱の損失
は最少とでき、熱の伝幡を最大限に利用できる。例えば
、焼付炉内で溶剤ガスのメタクレゾール、石油ナフサは
、次の燃焼熱を発生する。The strand W is passed through the paint tank 29 via the turn sheave 42 to coat its surface with paint, and then the die 27 adjusts the paint to a uniform layer thickness, and then the wire W is passed through the passage hole 26 into the sealed chamber. 24, and then passed through the lower opening 22 into the baking furnace 20 for baking, passed through the cooling chamber 41, cooled and solidified, and pulled out through the turn sheave 43 to produce an enameled insulated wire. is sealed in a closed chamber 24 to block outside air, and inside the baking furnace 20, high temperature air heated by the heat exchanger 37 blown from the passage 34a and solvent vapor generated inside the furnace 20 are mixed. Only the high temperature gas produced in the combustion furnace 30 with the mixed gas is circulated. Therefore, the air into the baking furnace 20 is high-temperature air that has been heat-exchanged by the necessary minimum amount of 8901/min through the passage 3.
It can be introduced from 4a, and the minimum amount of air required for exhaust is 890
1/min (23001/min at 450° C.), heat loss within the furnace 1 can be minimized and heat transmission can be utilized to the maximum. For example, the solvent gas metacresol and petroleum naphtha generate the following combustion heat in a baking furnace.
1P!
この燃焼熱は前記例として述べた製造条件で製造した場
合、l時間当り約45KWの電力に相当するエネルギー
が発生することになるが、前記のように本発明によれば
、このエネルギーを最小の損失で有効に利用できる。1P! When this combustion heat is manufactured under the manufacturing conditions described in the example above, energy equivalent to approximately 45 KW of electric power will be generated per hour, but as described above, according to the present invention, this energy can be minimized. Can be used effectively at a loss.
ところが従来のものは焼付炉の下部開口より外部の冷た
い空気が導入されるため、たとえ熱風を炉最下部まで循
環させる方式としても、必然的に炉の下部温度は低くく
なつてしまうし、それだけ熱エネルギーの損失も大にな
る。However, with conventional baking furnaces, cold air from outside is introduced through the opening at the bottom of the baking furnace, so even if hot air is circulated to the bottom of the furnace, the temperature at the bottom of the furnace will inevitably drop, and Thermal energy loss also increases.
また、本発明の如く焼付炉20の下部開口22を密封し
外部空気を遮断し、熱風の循環方式だと例えば上部45
0℃、中部450℃、下部450℃の設定が可能であり
、この条件下でもエナメル絶縁電線の特性に何ら差がな
いことを確認した。In addition, if the lower opening 22 of the baking furnace 20 is sealed to block external air as in the present invention, and if the hot air is circulated, for example, the upper opening 22 is sealed.
It was possible to set the temperature to 0°C, 450°C in the middle, and 450°C in the lower part, and it was confirmed that there was no difference in the characteristics of the enamel insulated wire even under these conditions.
更に、空気の流入が通路34からで排気が排出通路40
だけだから、空気の流入量及び排気量の制御も簡単であ
る。例えば、バルブの調整で簡単にできる。また、焼付
炉20の上部1ζおけるエアカーテン装置35には熱交
換器37で熱交換された高温の空気が使用されるから、
たとえ上部開口23における炉20内の上昇気流による
未燃焼分中の溶剤や重合物の凝縮を完全に防止でき、こ
の部分の清掃保守が不必要になつた。Furthermore, air inflows through the passage 34 and exhaust air flows through the exhaust passage 40.
Therefore, it is easy to control the amount of air inflow and air exhaust. For example, this can be easily done by adjusting the valve. Furthermore, since the air curtain device 35 in the upper part 1ζ of the baking furnace 20 uses high-temperature air heat-exchanged in the heat exchanger 37,
Even if it is possible to completely prevent the condensation of the solvent and polymers in the unburned matter due to the upward airflow inside the furnace 20 at the upper opening 23, cleaning and maintenance of this part is no longer necessary.
しかしながら、以上のような構造にしても並列する左右
の焼付炉20が構造的にも電気制御的にも同一の場合は
、炉20の片側をサイズ交換などで線掛作業を行なう時
密閉室24を開けたことによつて瞬間的に多量の空気が
炉20内に吸引され、炉20の温度変化がさらに顕著に
なるから、もう片側で製造中の製品に重大な悪影響を与
える。However, even with the above structure, if the parallel left and right baking furnaces 20 are the same in terms of structure and electrical control, when one side of the furnaces 20 is used for wire hanging work due to size exchange, etc., the sealed chamber 24 By opening the furnace 20, a large amount of air is instantly sucked into the furnace 20, and the temperature change in the furnace 20 becomes even more pronounced, which has a serious negative effect on the product being manufactured on the other side.
この問題を解決するため焼付炉20が左右完全に分離す
るか、一炉一サ・:″ズの焼付炉20を二炉併設する方
法を採用する。後者は設備費的に不利であるので通常は
前者を採用するのが得策である。例えば、その具体例を
示すと第3図及び第4図の如くである。第3図は中央縦
断面図、第4図は第3図A−A線断面図であり、同一符
号は第2図と同一のものを示す。以上説明したように本
発明は焼付炉の左右分割、焼付炉の下部開口の密閉、焼
付炉上部よりの最少必要空気量の導入及び熱風循環によ
るエネルギーの有効利用等により、焼付炉一台当り、前
記例として述べた製造条件でランニング電力量がl時間
当り25KW1製品のエナメル銅線1kf1を製造する
のに0.23KWHの電力消費量の実績を得た。To solve this problem, either the left and right sides of the baking furnace 20 are completely separated, or the two baking furnaces 20 of one size: It is advisable to adopt the former method. For example, specific examples thereof are shown in Figs. 3 and 4. Fig. 3 is a central vertical cross-sectional view, and Fig. 4 is a cross-sectional view of Fig. 3A-A. It is a line cross-sectional view, and the same reference numerals indicate the same parts as in Fig. 2.As explained above, the present invention is capable of dividing the baking furnace into left and right parts, sealing the lower opening of the baking furnace, and minimizing the amount of air required from the upper part of the baking furnace. With the introduction of a heating system and the effective use of energy through hot air circulation, it is possible to use 0.23 KWH per firing furnace to produce 1 kf1 of enamelled copper wire of 25 KW per 1 hour under the manufacturing conditions described in the example above. Obtained results on power consumption.
また、本発明はホルマール樹脂塗料のような溶剤分の多
い塗料については、当然炉内での燃焼熱の発生割合が多
くなるので、その電力消費料はさらに下がることが確か
められた。以上は電力によるヒーター加熱について説明
したが、本発明は可燃ガス、例えば都市ガス、L.N.
Gなどの燃焼熱を利用しても応用できることもちろんで
ある。尚、触媒32で燃焼する以前のメタクレゾールな
どの濃度は、最少必要空気量8901/分を炉20内に
導入した場合約2%となり、メタクレゾールの爆発下限
界濃度1.06%、を越えて何らかの原因で爆発する危
険性が生ずるので、触媒32でメタクレゾールなどが燃
焼する割合をl分間当り2回以上(通常は5〜15回)
の割合で燃焼するように炉20内にブロワ−36で強制
循環させ、絶対濃度を爆発下限界濃度以下で定常的に反
応するように設計する。Furthermore, in the present invention, it has been confirmed that for paints with a high solvent content, such as formal resin paints, the rate of combustion heat generated in the furnace naturally increases, so that the power consumption is further reduced. The above description has been about heater heating using electric power, but the present invention also applies to heating using combustible gas, such as city gas, L. N.
Of course, it can also be applied using combustion heat such as G. The concentration of metacresol etc. before combustion in the catalyst 32 is approximately 2% when the minimum required air flow rate of 8901/min is introduced into the furnace 20, which exceeds the lower explosive limit concentration of metacresol of 1.06%. Since there is a risk of explosion due to some reason, the rate at which meta-cresol etc. is burned in the catalyst 32 should be set at least 2 times per minute (usually 5 to 15 times).
The furnace 20 is forcibly circulated by a blower 36 so as to burn at a rate of 20%, and the reactor is designed to react steadily at an absolute concentration below the lower explosive limit concentration.
第1図は従来例を示す断面図、第2図は本発明の実施例
を示す中央縦断面図.第3図は焼付炉が左右分割型の場
合の実施例を示す中央縦断面図、第4図は第3図A−A
線断面図である。
20・・・・・・焼付炉、21・・・・・・ヒーター、
22・・・・・・下部開口、24・・・・・・密閉室、
30・・・・・・燃焼炉、32・・・・・・触媒、34
・・・・・・空気通路、35・・・・・・エアカーテン
装置、36・・・・・・ブロワ一、37・・・・・・熱
交換器、33・・・・・・通気路。Fig. 1 is a sectional view showing a conventional example, and Fig. 2 is a central longitudinal sectional view showing an embodiment of the present invention. Fig. 3 is a central vertical cross-sectional view showing an embodiment in which the baking furnace is of the left-right split type, and Fig. 4 is Fig. 3 A-A.
FIG. 20... Baking furnace, 21... Heater,
22... Lower opening, 24... Sealed chamber,
30... Combustion furnace, 32... Catalyst, 34
...Air passage, 35...Air curtain device, 36...Blower, 37...Heat exchanger, 33...Vent passage .
Claims (1)
イスを通して導体上のエナメル塗料層を所定の厚さに均
層化し、高温の焼付炉を通してエナメル塗料層の溶剤を
揮散、離脱させて導体上にエナメル塗料を焼付けた後、
エアカーテン装置及び冷却器を通して冷却するエナメル
絶縁電線の製造方法において、前記揮散、離脱させた溶
剤蒸気を前記焼付炉上部より炉外へ抜き出し、これにエ
アカーテン装置からの空気を混合し、これを燃焼して高
温ガスを作り、この高温ガスを前記溶剤蒸気混合用空気
の加熱に使用した後、その高温ガスの一部を前記焼付炉
の加熱に使用し、残部を系外へ排出するとともに、他方
前記高温ガスに加熱された空気は前記溶剤の燃焼に使用
するに先立ち前記焼付炉の出口に設けられたエアカーテ
ン装置のエアとして使用することを特徴とするエナメル
絶縁電線の製造方法。 2 下端に下部開口を、上端に上部開口を有する竪形焼
付炉の下方にダイス及び塗料槽を配し、上部開口近傍に
エアカーテン装置を設けてなるエナメル絶縁電線の製造
装置において、前記焼付炉の下部開口に密閉室を設ける
とともに、別途燃焼炉と熱交換器とを新設し、熱交換器
には空気入口を連結し、前記熱交換器とエアカーテン装
置との間、前記焼付炉の上部と前記燃焼炉との間、前記
燃焼炉と前記熱交換器との間及び前記熱交換器と前記焼
付炉の下部あるいは前記密閉室との間にそれぞれ通気路
を設けてなるエナメル絶縁電線の製造装置。 3 前記燃焼炉として前記燃焼炉の前記エアカーテン装
置側通気路側からブロアー及び酸化触媒を配置内蔵して
なる燃焼炉を設けてなる特許請求の範囲第2項記載のエ
ナメル絶縁電線の製造装置。[Claims] 1. Applying enamel paint onto the conductor through a paint tank, homogenizing the enamel paint layer on the conductor to a predetermined thickness through a die, and volatilizing the solvent in the enamel paint layer through a high-temperature baking furnace. After separating and baking enamel paint on the conductor,
In a method for manufacturing an enameled insulated wire that is cooled through an air curtain device and a cooler, the volatilized and released solvent vapor is extracted from the upper part of the baking furnace to the outside of the furnace, and air from the air curtain device is mixed with it. After burning to produce high-temperature gas and using this high-temperature gas to heat the solvent vapor mixing air, a part of the high-temperature gas is used to heat the baking furnace, and the remainder is discharged to the outside of the system, On the other hand, a method for producing an enameled insulated wire, characterized in that the air heated by the high-temperature gas is used as air for an air curtain device provided at the outlet of the baking furnace before being used for combustion of the solvent. 2. An enameled insulated wire manufacturing apparatus comprising a vertical baking furnace having a lower opening at the lower end and an upper opening at the upper end, a die and a paint tank disposed below the baking furnace, and an air curtain device near the upper opening. At the same time, a combustion furnace and a heat exchanger are installed separately, an air inlet is connected to the heat exchanger, and a closed chamber is provided at the lower opening of the baking furnace. and the combustion furnace, between the combustion furnace and the heat exchanger, and between the heat exchanger and the lower part of the baking furnace or the sealed chamber. Device. 3. The apparatus for manufacturing an enameled insulated wire according to claim 2, wherein the combustion furnace is a combustion furnace in which a blower and an oxidation catalyst are disposed and built in from the air passage side of the air curtain device side of the combustion furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1765181A JPS5919613B2 (en) | 1981-02-09 | 1981-02-09 | Method for manufacturing enamel insulated wire and equipment for manufacturing the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1765181A JPS5919613B2 (en) | 1981-02-09 | 1981-02-09 | Method for manufacturing enamel insulated wire and equipment for manufacturing the same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57132611A JPS57132611A (en) | 1982-08-17 |
| JPS5919613B2 true JPS5919613B2 (en) | 1984-05-08 |
Family
ID=11949751
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1765181A Expired JPS5919613B2 (en) | 1981-02-09 | 1981-02-09 | Method for manufacturing enamel insulated wire and equipment for manufacturing the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5919613B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63130512U (en) * | 1987-02-20 | 1988-08-26 |
-
1981
- 1981-02-09 JP JP1765181A patent/JPS5919613B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63130512U (en) * | 1987-02-20 | 1988-08-26 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57132611A (en) | 1982-08-17 |
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