JPH0629380B2 - Manufacturing method of electrical insulation paint - Google Patents

Manufacturing method of electrical insulation paint

Info

Publication number
JPH0629380B2
JPH0629380B2 JP60096299A JP9629985A JPH0629380B2 JP H0629380 B2 JPH0629380 B2 JP H0629380B2 JP 60096299 A JP60096299 A JP 60096299A JP 9629985 A JP9629985 A JP 9629985A JP H0629380 B2 JPH0629380 B2 JP H0629380B2
Authority
JP
Japan
Prior art keywords
molecular weight
acid
polyhydric alcohol
resin
reaction
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 - Lifetime
Application number
JP60096299A
Other languages
Japanese (ja)
Other versions
JPS61254674A (en
Inventor
泰典 岡田
正三 葛西
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Resonac Corp
Original Assignee
Hitachi Chemical Co Ltd
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 by Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP60096299A priority Critical patent/JPH0629380B2/en
Publication of JPS61254674A publication Critical patent/JPS61254674A/en
Publication of JPH0629380B2 publication Critical patent/JPH0629380B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Polyesters Or Polycarbonates (AREA)
  • Paints Or Removers (AREA)
  • Organic Insulating Materials (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は高速で塗装焼付ができ,エナメル線の生産効率
を大幅に向上されることができる電気絶縁塗料の製造法
に関する。
Description: TECHNICAL FIELD The present invention relates to a method for producing an electrically insulating paint capable of coating baking at high speed and greatly improving the production efficiency of an enameled wire.

(従来の技術) エナメル線の製造速度を速くし,生産性をあげることに
よつてコストダウンを図るとともに,顧客の要求に迅速
に対応してサービス向上を図ることを目的として,高速
で塗装焼付が可能なエナメル線用ポリエステル系電気絶
縁塗料(以下,単に電気絶縁塗料と略す)の開発が望ま
れている。
(Prior Art) High-speed paint baking for the purpose of speeding up the production of enameled wire and improving the productivity to reduce costs, as well as quickly responding to customer requests and improving services. It is desired to develop a polyester-based electric insulating paint for enamel wire (hereinafter simply referred to as electric insulating paint) that can be used.

従来からある絶縁塗料をそのまま高速で焼付けた場合に
は塗膜の硬化度が不十分なために例えばカツトスルー温
度,耐摩耗性などの特性が低下するとともに,硬化度が
不十分なまま多層に塗布焼付けをくり返すために塗膜が
部分的に軟化流動し,発泡や凹凸が発生して表面の平滑
性が失われる結果となる。
When the conventional insulating paint is baked at high speed as it is, the curing degree of the coating film is insufficient, so that the properties such as cut-through temperature and abrasion resistance are degraded, and it is applied in multiple layers while the curing degree is insufficient. Due to repeated baking, the coating film partially softens and flows, causing foaming and unevenness, resulting in loss of surface smoothness.

焼付炉温を高くすれば硬化度があがり,カツトスルー温
度,耐摩耗性などの特性は合格範囲に入るが,炉温が高
いために焼付時の揮発性成分の量が増加し,エナメル線
の表面に発泡が生じ易くなる。また,炉温を高くするた
めにはその分だけ余計にエネルギーが必要となり,コス
トダウンの目的とは逆行する。このような不都合を避け
るために,従来型の絶縁塗料にポリアミド樹脂,フエノ
ール樹脂,メラミン樹脂などの二次樹脂を添加したり,
触媒作用を有する各種金属塩などを多量に添加する方法
などが試みられているが,エナメル線の特性と外観の両
方を満足させるものは得られていない。
If the baking oven temperature is raised, the degree of hardening rises, and the characteristics such as cut-through temperature and wear resistance fall within the acceptable range, but since the furnace temperature is high, the amount of volatile components during baking increases and the surface of the enamel wire increases. Foaming easily occurs. In addition, in order to raise the furnace temperature, extra energy is required, which is contrary to the purpose of cost reduction. In order to avoid such inconvenience, secondary resin such as polyamide resin, phenol resin, melamine resin is added to conventional insulating paint,
Attempts have been made to add a large amount of various metal salts having a catalytic action, but none have been obtained that satisfy both the characteristics and appearance of enameled wire.

(発明が解決しようとする問題点) 本発明はこのような問題点を解決するためになされたも
ので,エナメル線の諸特性並びに外観は従来品と同等以
上でかつ,塗装焼付速度を従来品よりも20〜30%以
上速くすることが可能な電気絶縁塗料の製造法を提供す
ることを目的とする。
(Problems to be Solved by the Invention) The present invention has been made to solve such problems, and the characteristics and appearance of the enameled wire are equal to or higher than those of the conventional product, and the coating baking speed is the same as that of the conventional product. It is an object of the present invention to provide a method for producing an electrically insulating coating which can be made 20 to 30% faster than the above.

(問題点を解決するための手段) 本発明は多価カルボン酸またはその誘導体と多価アルコ
ールとを三価以上の多価アルコールを全多価アルコール
の50当量%以上としてカルボキシル基の反応率が70
%以上になるまで反応させた後,さらに好ましくは触媒
の存在下にポリスチレン換算の数平均分子量が1500
〜1700になるまで130〜200℃で加熱反応させ
て得られた樹脂を有機溶剤に溶解させる電気絶縁塗料の
製造法に関する。
(Means for Solving Problems) In the present invention, the polycarboxylic acid or its derivative and the polyhydric alcohol are trivalent or higher polyhydric alcohols in an amount of 50 equivalent% or more based on the total polyhydric alcohol, and the reaction rate of the carboxyl group is 70
%, The number average molecular weight in terms of polystyrene is more preferably 1500 in the presence of a catalyst.
The present invention relates to a method for producing an electrically insulating coating material in which a resin obtained by heating and reacting at 130 to 200 ° C. until dissolved in an organic solvent is dissolved in an organic solvent.

多価カルボン酸の例としてはテレフタル酸,イソフタル
酸,フタル酸,トリメリツト酸,ピロメリツト酸,トリ
メシン酸,ビシクロー〔2,2,2〕−オクト−(7)−
エン−2:3:5:6−テトラカルボン酸,1,2,
3,4−ブタンテトラカルボン酸,1,2,3−ブタト
リカルボン酸,1,2,4−ブタントリカルボン酸,ア
ジピン酸,コハク酸,セバシン酸などがあげられ特に制
限はない。また,イミド酸形成成分であるジアミン又は
アミノカルボン酸と三塩基酸無水物とを最初に加えても
よいし,別途合成したイミド酸として加えてもよい。多
価カルボン酸の誘導体とはこれらの酸の無水物,エステ
ル,クロライドを指す。
Examples of polycarboxylic acids are terephthalic acid, isophthalic acid, phthalic acid, trimellitic acid, pyromellitic acid, trimesic acid, bicyclo- [2,2,2] -oct- (7)-
En-2: 3: 5: 6-tetracarboxylic acid, 1,2,
3,4-butanetetracarboxylic acid, 1,2,3-butatricarboxylic acid, 1,2,4-butanetricarboxylic acid, adipic acid, succinic acid, sebacic acid and the like are mentioned and not particularly limited. Moreover, the diamine or aminocarboxylic acid which is an imidic acid-forming component and the tribasic acid anhydride may be added first, or may be added as a separately synthesized imidic acid. Derivatives of polycarboxylic acids refer to anhydrides, esters and chlorides of these acids.

多価アルコールとしてはエチレングリコール,プロピレ
ングリコール,ジプロピレングリコール,1,3−ブタ
ンジオール,1,6−ヘキサジオール,ジエチレングリ
コール,ネオペンチルグリコール,グリセリン,トリス
(2−ヒドロキシエチルイソシアヌレート)トリメチロ
ールプロパン,トリメチロールエタン,ペンタエリスト
リール,ソルビトールなどがあげられる。
Examples of polyhydric alcohols are ethylene glycol, propylene glycol, dipropylene glycol, 1,3-butanediol, 1,6-hexadiol, diethylene glycol, neopentyl glycol, glycerin, tris (2-hydroxyethyl isocyanurate) trimethylolpropane, Examples include trimethylolethane, pentaerythritol, and sorbitol.

多価カルボン酸またはその誘導体と多価アルコールとは
以下に述べる条件以外は,通常の方法によつて反応させ
ることができ,特に制限はない。反応には触媒を用いる
ことが好ましく,それによつて短時間に反応を進めるこ
とができる。
The polyvalent carboxylic acid or its derivative and the polyhydric alcohol can be reacted by an ordinary method except the conditions described below, and there is no particular limitation. It is preferable to use a catalyst for the reaction, which allows the reaction to proceed in a short time.

多価カルボン酸またはその誘導体と多価アルコールとを
反応させるに際し,三価以上の多価アルコールを全多価
アルコールの50当量%以上とする必要がある。三価以
上の多価アルコールが50当量%未満の場合には焼付後
の塗膜の架橋密度が不十分になり,カツトスルー温度や
耐摩耗性などの特性が劣る。また,80当量%を越えた
場合には可とう性が低下する傾向にあるため,三価以上
の多価アルコールの使用量は80当量%以下が好まし
く,カツトスルー温度や可とう性のバランスを考慮する
と55〜65当量%の範囲にすることが特に好ましい。
When the polyhydric carboxylic acid or its derivative is reacted with the polyhydric alcohol, the polyhydric alcohol having a valence of 3 or more must be 50 equivalent% or more of the total polyhydric alcohol. If the amount of the trihydric or higher polyhydric alcohol is less than 50 equivalent%, the cross-linking density of the coating film after baking will be insufficient, and the properties such as cut-through temperature and abrasion resistance will be poor. Also, when the amount exceeds 80 equivalent%, the flexibility tends to decrease. Therefore, it is preferable to use trihydric or higher polyhydric alcohol in an amount of 80 equivalent% or less. Consider the cut-through temperature and the balance of flexibility. Then, it is particularly preferable to set it in the range of 55 to 65 equivalent%.

水酸基とカルボキシル基の当量比(OH/COOH)は1.1
0〜1.40が好ましく,1.20〜1.30とするの
が特に好ましい。1.10未満では一段目の反応で分子
量が大きくなり過ぎ,分子量分布の均一化が困難であ
り,1.40を越えた場合には未反応の多価アルコール
の残存量が多くなる。
Equivalent ratio of hydroxyl group to carboxyl group (OH / COOH) is 1.1
0 to 1.40 is preferable, and 1.20 to 1.30 is particularly preferable. If it is less than 1.10, the molecular weight becomes too large in the first-step reaction, and it is difficult to make the molecular weight distribution uniform. If it exceeds 1.40, the amount of unreacted polyhydric alcohol remaining increases.

多価カルボン酸またはその誘導体の多価アルコールとは
カルボキシル基の反応率が70%以上になるまで反応さ
せる必要がある。反応率が70%未満では未反応の多価
カルボン酸またはその誘導体並びに多価アルコールの残
存率が多く,また,低分子のオリゴマの量が多いため
に,エナメル線の特性が不十分になるばかりでなく,こ
れらの低分子成分が焼付時に揮発してエナメル線の表面
に凹凸が生成し易くなる。反応率はできるだけ高い方が
よいが,三価以上の多価アルコールの使用量が多くなる
とゲル化の危険性もあり,総合的に判断すると75〜8
0%とするのが特に好ましい。
It is necessary to react with the polyhydric carboxylic acid or the polyhydric alcohol of its derivative until the reaction rate of the carboxyl group becomes 70% or more. If the reaction rate is less than 70%, the residual rate of unreacted polycarboxylic acid or its derivative and polyhydric alcohol is high, and the amount of low molecular weight oligomers is large, so that the characteristics of the enameled wire are not sufficient. Not only that, these low-molecular components volatilize during baking, making it easier to produce irregularities on the surface of the enamel wire. The reaction rate should be as high as possible, but there is a risk of gelation when the amount of trihydric or higher polyhydric alcohol used is large.
It is particularly preferably set to 0%.

カルボキシル基の反応率は酸価の測定や,副生物である
水,アルコールなどの量を測定することによつて良く知
られた方法で求めることができる。
The reaction rate of the carboxyl group can be determined by a well-known method by measuring the acid value and the amount of by-products such as water and alcohol.

反応が終了したら冷却して溶剤を加え,溶解する。使用
できる溶剤の例としてはキシレノール,クレゾール,フ
エノール,N−メチル−2−ピロリドン,N,N−ジメ
チルホルムアミド,N,N−ジメチルアセトアミド,キ
シレン,芳香族炭化水素(例えば日本石油製ハイゾール
100,ハイゾール150)などがあげられる。後述の
特に好ましい反応温度である150〜170℃の条件及
びコスト等を考慮すると,溶媒としてはキシレノール,
クレゾール,フエノールおよび沸点が150℃を越える
芳香族炭化水素を用いることが好ましい。そのまま13
0〜200℃に加熱してもよいが,それでは樹脂のポリ
スチレン換算の数平均分子量が1500〜1700にな
るまでに時間を要するので,触媒を添加することが好ま
しい。触媒としてはテトラブチルチタネート,テトライ
ソプロピルチタネートなどのチタニウムアルコラート,
アルミニウムイソプロピレート,アルミニウムブチレー
トなどのアルミニウムアルコラート,ジルコニウムアル
コラートなどのほか,これらの化合物から誘導されるβ
−ジケトンやケトエステルとの錯体などがあげられ,こ
れらの化合物を樹脂に対して0.1〜5重量%加えるこ
とが好ましく,1〜3重量%とすることがより好まし
い。添加量が0.1重量%未満では反応の促進硬化が乏
しく,5重量%を越えた場合にはエナメル線の可とう性
が低下する傾向がある。130〜200℃に加熱した際
に起こる反応の内容については十分明らかではないが,
平均分子量が小さくなり,かつ分子量分布が平均化され
る反応であつて,下記に示したように,ポリエステル樹
脂が触媒として加えた金属アルコラート,溶媒として加
えたフエノール類,系中の水分などと反応しているもの
と推定される。金属アルコラート自身が反応している場
合には厳密な意味での触媒の定義からはずれるが,ここ
では金属アルコラートは広義に触媒として解釈する。
When the reaction is complete, cool and add the solvent to dissolve. Examples of the solvent that can be used are xylenol, cresol, phenol, N-methyl-2-pyrrolidone, N, N-dimethylformamide, N, N-dimethylacetamide, xylene, and aromatic hydrocarbons (for example, Hysol 100 manufactured by Nippon Oil Co., Hisol. 150) and the like. Considering the conditions of 150 to 170 ° C., which is a particularly preferable reaction temperature described later, and cost, xylenol is used as a solvent,
Preference is given to using cresol, phenol and aromatic hydrocarbons having a boiling point above 150 ° C. As it is 13
Although it may be heated to 0 to 200 ° C., it takes time until the polystyrene-reduced number average molecular weight of the resin becomes 1500 to 1700, so it is preferable to add a catalyst. Titanium alcoholates such as tetrabutyl titanate and tetraisopropyl titanate are used as catalysts,
In addition to aluminum alcoholates such as aluminum isopropylate and aluminum butyrate, zirconium alcoholates, β derived from these compounds
Examples thereof include complexes with diketones and ketoesters, and these compounds are preferably added in an amount of 0.1 to 5% by weight, more preferably 1 to 3% by weight, based on the resin. If the addition amount is less than 0.1% by weight, the accelerated curing of the reaction is poor, and if it exceeds 5% by weight, the flexibility of the enamel wire tends to decrease. Although the content of the reaction that occurs when heated to 130 to 200 ° C is not clear enough,
As shown below, polyester resin reacts with metal alcoholate added as a catalyst, phenols added as a solvent, water in the system, etc., as the average molecular weight is reduced and the molecular weight distribution is averaged. It is presumed that When the metal alcoholate itself is reacting, it is outside the definition of a catalyst in a strict sense, but here, the metal alcoholate is broadly interpreted as a catalyst.

反応温度は130〜200℃とされる。130℃未満で
は分子量分布均一化の反応速度が極めて遅くなる。ま
た,200℃を越えた場合には分子量分布均一化のみな
らず,逆の分子量増大反応も同時に起こり,目的とする
電気絶縁塗料が得られなくなる。これらのこと及び,反
応の制御のし易さなどを考慮すると140〜180℃が
より好ましく,150〜170℃が特に好ましい。
The reaction temperature is 130 to 200 ° C. If the temperature is lower than 130 ° C., the reaction rate for homogenizing the molecular weight distribution becomes extremely slow. Further, when the temperature exceeds 200 ° C., not only the molecular weight distribution becomes uniform, but also the opposite molecular weight increasing reaction occurs at the same time, so that the intended electrically insulating coating cannot be obtained. Considering these and the ease of controlling the reaction, 140 to 180 ° C is more preferable, and 150 to 170 ° C is particularly preferable.

このような温度でポリスチレン換算の数平均分子量が1
500〜1700になるまで,反応させる。数平均分子
量が1700を越えた場合にはメナメル線の表面に凹凸
が生じ易くなり,1500未満の場合にはカツトスルー
温度や耐摩耗性が低下する。数平均分子量は例えばカラ
ム:日立化成工業(株)製ゲルパツク,R420,R4
30,R440;溶出溶剤:テトラヒドロフラン;検出
器:示差屈折計;圧力:40kgf/cm2,温度:350
℃,流速:2.0ml/min の条件で液体クロマトグラフ
イー(HLC)によつて分子量分布を測定し,別途作成
したポリスチレンの検量線を用いて常法によつて算出す
ることができる。樹脂の溶液粘度と数平均分子量との相
関曲線をあらかじめ作成しておけば,反応系からサンプ
リングした溶液の粘度を測定することによつて簡便に反
応の制御を行なうことができる。ちなみに,加熱処理前
の樹脂のHLCクロマトグラムには2つの主ピークがあ
り,数平均分子量は2,000−2,500であるが,
1500〜1700になるまで加熱処理した後では主ピ
ークが一つで,全体的な形状は加熱処理前と比べると遥
かに正規分布に近くなつている。このように分子量分布
が平均化されるため硬化が均一に起こり,高速で塗装焼
付してもエナメル線の方面に凹凸が生じず,平滑で均質
な塗膜を形成するものと考えられる。
At such a temperature, the polystyrene-equivalent number average molecular weight is 1
React until 500-1700. When the number average molecular weight exceeds 1700, unevenness is likely to occur on the surface of the menamel wire, and when it is less than 1500, the cut-through temperature and abrasion resistance decrease. The number average molecular weight is, for example, a column: gel pack, R420, R4 manufactured by Hitachi Chemical Co., Ltd.
30, R440; elution solvent: tetrahydrofuran; detector: differential refractometer; pressure: 40 kgf / cm 2 , temperature: 350
The molecular weight distribution can be measured by liquid chromatography (HLC) under the conditions of ° C and a flow rate of 2.0 ml / min, and can be calculated by a conventional method using a separately prepared calibration curve of polystyrene. If a correlation curve between the solution viscosity of the resin and the number average molecular weight is prepared in advance, the reaction can be easily controlled by measuring the viscosity of the solution sampled from the reaction system. By the way, the HLC chromatogram of the resin before heat treatment has two main peaks, and the number average molecular weight is 2,000-2,500.
There is one main peak after heat treatment until it reaches 1500 to 1700, and the overall shape is much closer to the normal distribution as compared with before heat treatment. It is considered that since the molecular weight distribution is averaged in this way, curing uniformly occurs, and even if the coating is baked at high speed, no unevenness is generated on the surface of the enamel wire, and a smooth and uniform coating film is formed.

このようにして得られた電気絶縁塗料をそのまま,ある
いは前述して溶剤で更に希釈して実用に供する。
The electric insulating coating material thus obtained is used as it is, or is diluted with a solvent as described above for practical use.

なお,電気絶縁塗料の焼付時の硬化性及びエナメル線の
特性の向上を目的として各種の添加剤を加えることがで
きる。そのような添加剤の例としてはナフテン酸亜鉛,
オクテン酸亜鉛,ナフテン酸コバルト,オクテン酸鉄な
どの有機酸の金属塩,前述したチタニウム,アルミニウ
ム,ジルコニウムなどの金属アルコラート及びその錯体
などの誘導体のほか,メラミン樹脂,フエノール樹脂,
キシレン樹脂,フラン樹脂,エポキシ樹脂,ポリアミド
樹脂などがあげられ,エナメル線の加熱変色性を改善す
る観点からメラミン樹脂,フエノール樹脂を用いること
が好ましい。
Various additives may be added for the purpose of improving the curability of the electrically insulating paint during baking and the characteristics of the enameled wire. Examples of such additives include zinc naphthenate,
In addition to metal salts of organic acids such as zinc octenoate, cobalt naphthenate, iron octenoate, the aforementioned metal alcoholates such as titanium, aluminum, zirconium and their derivatives, melamine resin, phenol resin,
Examples of the resin include xylene resin, furan resin, epoxy resin and polyamide resin, and it is preferable to use melamine resin and phenol resin from the viewpoint of improving the heat discoloration of the enamel wire.

(発明の効果) 本発明の製造法によつて得られた電気絶縁塗料を用いる
ことにより上記した諸問題を解消してエナメル綿製造メ
ーカの最近の強い要望に応えることができる。
(Effects of the Invention) By using the electrically insulating coating material obtained by the production method of the present invention, it is possible to solve the above-mentioned problems and meet the recent strong demands of enamel cotton manufacturers.

(実施例) 以下,本発明を実施例によつて更に詳細に説明するが,
本発明はこれらの実施例に限定されるものでないことは
言うまでもない。
(Examples) Hereinafter, the present invention will be described in more detail with reference to Examples.
It goes without saying that the invention is not limited to these examples.

実施例1 撹拌機,窒素導入管,温度計,冷却器を備えた3のフ
ラスコにテレフタル酸ジメチル945g,イソフタル酸
202g,グリセリン257g,エチレングリコール2
12g,酢酸鉛0.95gを入れ,170℃で6時間反
応させた後,3時間かけて225℃まで昇温し,この温
度で留出液の量が292g(反応率=82%,副生物で
あるメタノールと水との生成量から算出した。以下実施
例,比較例においても同じ。)になるまで反応を続け
た。その後,急冷してクレゾール1568gを加えた。
この溶液から1400gをとりテトラブチルチタネート
12.5gを加え,155℃で数平均分子量が1680
(前記の方法によつて測定,以下の実施例においても同
じ)になるまで加熱反応させた。その後,キシレン33
3gを加えて希釈した。
Example 1 In a flask 3 equipped with a stirrer, a nitrogen inlet tube, a thermometer, and a condenser, 945 g of dimethyl terephthalate, 202 g of isophthalic acid, 257 g of glycerin, and ethylene glycol 2
After adding 12g and 0.95g of lead acetate and reacting at 170 ° C for 6 hours, the temperature was raised to 225 ° C over 3 hours. At this temperature, the amount of distillate was 292g (reaction rate = 82%, by-product). It was calculated from the amount of methanol and water produced, which was the same in the following Examples and Comparative Examples). Then, it was rapidly cooled and 1568 g of cresol was added.
1400 g of this solution was added to 12.5 g of tetrabutyl titanate, and the number average molecular weight was 1680 at 155 ° C.
The reaction was carried out by heating until (measured by the above method, the same applies to the following examples). Then xylene 33
3 g was added and diluted.

実施例2 実施例1と同様にしてテレフタル酸ジメチル832g,
イソフタル酸79g,グリセリン211g,エチレング
リコール142g,酢酸鉛0.87gを反応率が79%
になるまで反応させた。その後クレゾール972g及び
テトラブチルチタネート14.6gを加え,160℃で
数平均分子量が1590になるまで加熱反応させた。更
に,ハイゾール100を432g,日立化成工業(株)
製フエノール樹脂VP−51NY,1.0gを加えた。
Example 2 In the same manner as in Example 1, 832 g of dimethyl terephthalate,
79% isophthalic acid, 211 g glycerin, 142 g ethylene glycol, 0.87 g lead acetate with a reaction rate of 79%
It was made to react until it became. Thereafter, 972 g of cresol and 14.6 g of tetrabutyl titanate were added, and the mixture was heated and reacted at 160 ° C. until the number average molecular weight became 1590. Furthermore, 432 g of Hisol 100, Hitachi Chemical Co., Ltd.
A phenol resin VP-51NY (1.0 g, manufactured) was added.

実施例3 実施例1と同様にしてテレフタル酸ジメチル925g,
グリセリン228g,エチレングリコール124g,酢
酸鉛0.93gを反応率が76%になるまで反応させ
た。その後,クレゾール1210g,テトライソプロピ
ルチタネート19gを加え,165℃で数平均分子量が
1510になるまで反応させ,更にハイゾール100
519g,日立化成工業(株)製メラミン樹脂ML−5
23を1.0g加えた。
Example 3 In the same manner as in Example 1, 925 g of dimethyl terephthalate,
Glycerin (228 g), ethylene glycol (124 g) and lead acetate (0.93 g) were reacted until the reaction rate reached 76%. Then, 1210 g of cresol and 19 g of tetraisopropyl titanate were added and reacted at 165 ° C. until the number average molecular weight became 1510.
519 g, Hitachi Chemical Co., Ltd. melamine resin ML-5
1.0 g of 23 was added.

比較例1 実施例1で多価アルコールと多塩基酸とを反応率が82
%になるまで反応後,クレゾール1568gを加えて得られ
た溶液から1400gをとり,これにテトラブチルチタ
ネート12.5g,キシレン333gを加えて希釈し
た。
Comparative Example 1 The reaction rate of polyhydric alcohol and polybasic acid in Example 1 was 82.
After the reaction was completed to 1%, 1568 g of cresol was added to obtain a solution of 1400 g, which was diluted with 12.5 g of tetrabutyl titanate and 333 g of xylene.

比較例2 従来品の一例として日立化成工業(株)製WH−406
を用いた。
Comparative Example 2 As an example of conventional products, WH-406 manufactured by Hitachi Chemical Co., Ltd.
Was used.

実施例1〜3及び比較例1〜2の塗料を常法により,フ
エルトを用いて直径0.2mmの銅線に塗布し,炉温40
0/500℃(入口/出口)で焼付けることを6回繰り
返して得られた仕上り外径0.242mmのエナメル線の
特性を表1に示した。
The coating materials of Examples 1 to 3 and Comparative Examples 1 and 2 were applied to a copper wire having a diameter of 0.2 mm by using a felt by a conventional method, and a furnace temperature of 40
Table 1 shows the characteristics of an enameled wire with a finished outer diameter of 0.242 mm obtained by repeating baking at 0/500 ° C. (inlet / outlet) 6 times.

1) 外観評価,A:表面平滑で良好,B:若干凹凸があ
るが大むね良好,C:凹凸著しく不良。
1) Appearance evaluation, A: The surface is smooth and good, B: There are some irregularities but it is generally good, and C: The irregularities are extremely poor.

2) その他はJIS C 3003に準じて評価した。2) Others were evaluated according to JIS C 3003.

表1に示したように,本発明によつて得られる電気絶縁
塗料を用いた場合には,エナメル線の諸特性をはじめ,
表面の平滑性を損うことなく,従来型の電気絶縁塗料や
分子量分布の均一化を行なわない塗料を用いた場合より
も,焼付速度を25〜30%も速くすることができ,メ
ナメル線の製造工程の合理化に大きく貢献することがで
きる。
As shown in Table 1, when the electrical insulating coating obtained according to the present invention is used, various characteristics of the enamel wire,
The baking speed can be increased by 25 to 30% as compared with the case of using the conventional electric insulating paint or the paint that does not make the molecular weight distribution uniform without impairing the smoothness of the surface. It can greatly contribute to the rationalization of the manufacturing process.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】多価カルボン酸またはその誘導体と多価ア
ルコールとを三価以上の多価アルコールを全多価アルコ
ールの50当量%以上としてカルボキシル基の反応率が
70%以上になるまで反応させた後,さらに,好ましく
は触媒の存在下にポリスチレン換算の数平均分子量が1
500〜1700になるまで130〜200℃で加熱反
応させて得られた樹脂を有機溶剤に溶解させること特徴
とする電気絶縁塗料の製造法。
1. A polyhydric carboxylic acid or its derivative and a polyhydric alcohol are allowed to react until the reaction rate of a carboxyl group becomes 70% or more with trivalent or more polyhydric alcohol being 50 equivalent% or more of all polyhydric alcohols. Further preferably, the polystyrene reduced number average molecular weight is 1 in the presence of a catalyst.
A method for producing an electrically insulating coating material, which comprises dissolving a resin obtained by heating and reacting at 130 to 200 ° C. to 500 to 1700 in an organic solvent.
JP60096299A 1985-05-07 1985-05-07 Manufacturing method of electrical insulation paint Expired - Lifetime JPH0629380B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60096299A JPH0629380B2 (en) 1985-05-07 1985-05-07 Manufacturing method of electrical insulation paint

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60096299A JPH0629380B2 (en) 1985-05-07 1985-05-07 Manufacturing method of electrical insulation paint

Publications (2)

Publication Number Publication Date
JPS61254674A JPS61254674A (en) 1986-11-12
JPH0629380B2 true JPH0629380B2 (en) 1994-04-20

Family

ID=14161154

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60096299A Expired - Lifetime JPH0629380B2 (en) 1985-05-07 1985-05-07 Manufacturing method of electrical insulation paint

Country Status (1)

Country Link
JP (1) JPH0629380B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0794542B2 (en) * 1987-05-08 1995-10-11 大日精化工業株式会社 Polyester imide resin
JPH07100768B2 (en) * 1987-09-04 1995-11-01 大日精化工業株式会社 Polyester insulation paint

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5756506B2 (en) * 1974-05-30 1982-11-30

Also Published As

Publication number Publication date
JPS61254674A (en) 1986-11-12

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