JPS63221037A - Oil-immersed electric insulating polypropylene film and manufacture thereof - Google Patents

Oil-immersed electric insulating polypropylene film and manufacture thereof

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Publication number
JPS63221037A
JPS63221037A JP5458187A JP5458187A JPS63221037A JP S63221037 A JPS63221037 A JP S63221037A JP 5458187 A JP5458187 A JP 5458187A JP 5458187 A JP5458187 A JP 5458187A JP S63221037 A JPS63221037 A JP S63221037A
Authority
JP
Japan
Prior art keywords
oil
layer
polypropylene
film
immersed
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.)
Granted
Application number
JP5458187A
Other languages
Japanese (ja)
Other versions
JPH074899B2 (en
Inventor
渡辺 愼一
達也 伊藤
勝洋 土屋
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP5458187A priority Critical patent/JPH074899B2/en
Publication of JPS63221037A publication Critical patent/JPS63221037A/en
Publication of JPH074899B2 publication Critical patent/JPH074899B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Laminated Bodies (AREA)
  • Fixed Capacitors And Capacitor Manufacturing Machines (AREA)
  • Insulating Bodies (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は電気絶縁油に浸漬して、コンデンサ、電カケー
プル、トランス等の絶縁層として使用されるプロピレン
フィルム及びその製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a propylene film that is immersed in electrical insulating oil and used as an insulating layer for capacitors, power cables, transformers, etc., and a method for producing the same.

[従来の技術] ポリプロピレンフィルムは、優れた電気絶縁性を有し、
しかも軽量であるため絶縁紙に代わって電カケープル、
コンデンサ、トランスなどに利用されるようになった。
[Prior art] Polypropylene film has excellent electrical insulation properties,
Moreover, because it is lightweight, electric cable can be used instead of insulating paper.
It has come to be used in capacitors, transformers, etc.

しかしながら、ポリプロピレンフィルムは表面における
電気絶縁油(以下、油と記す)の拡散性が悪く、該フィ
ルムを例えばコンデンサの絶縁紙に代えて用いた場合、
油の含浸速度が遅く、均一に含浸されないという問題が
あり、該フィルムの表面を粗面化して油の拡散性を改良
する方法が種々提案されている〈例えば、特開昭51−
63500号公報、特公昭61−5733:3@公報、
特公昭61−26168号公報など)。
However, polypropylene film has poor diffusion of electrical insulating oil (hereinafter referred to as oil) on its surface, and when this film is used in place of insulating paper in a capacitor, for example,
There is a problem that the oil impregnation speed is slow and the oil is not impregnated uniformly, and various methods have been proposed to roughen the surface of the film and improve the oil dispersion (for example, Japanese Patent Application Laid-Open No. 1983-1993).
Publication No. 63500, Special Publication No. 61-5733:3 @ Publication,
(Special Publication No. 61-26168, etc.).

[発明が解決しようとする問題点] しかしながら、従来の粗面化ポリプロピレンフィルムは
油に対する膨潤が極めて大きいという欠点があり、油に
含浸した場合、膨潤により部分的に厚さ方向に変形を起
こして、フィルム層間が密着して油の補給路を遮断し、
このために絶縁破壊電圧が低下したり、発熱等により素
子が短時間で破壊する問題点があった。
[Problems to be Solved by the Invention] However, the conventional roughened polypropylene film has the drawback of extremely large swelling in oil, and when impregnated with oil, it partially deforms in the thickness direction due to swelling. , the film layers come into close contact and cut off the oil supply route,
For this reason, there are problems in that the dielectric breakdown voltage decreases and the element breaks down in a short period of time due to heat generation and the like.

本発明は、かかる問題点を改善し、油含浸性に優れ、か
つ油膨潤変形の小さい油浸電気絶縁用ポリプロピレンフ
ィルム及びその製造方法を提供することを目的とする。
An object of the present invention is to improve such problems and provide an oil-immersed electrically insulating polypropylene film that has excellent oil impregnability and small oil swelling deformation, and a method for producing the same.

「問題点を解決するための手段」 本発明は、実質的に空孔を含有しないポリプロピレン層
(I>の少なくとも片面に空孔率が30〜85%、平均
孔径が0.01〜5μmである多孔質ポリプロピレン層
(H)が積層され、かつ(1)層の厚み分率が50〜9
0%であることを特徴とする油浸電気絶縁用ポリプロピ
レンフィルム、及びその製造方法に関するものである。
"Means for Solving the Problems" The present invention provides a polypropylene layer (I) which contains substantially no pores, has a porosity of 30 to 85% on at least one side, and an average pore diameter of 0.01 to 5 μm. The porous polypropylene layer (H) is laminated, and the thickness fraction of the (1) layer is 50 to 9.
The present invention relates to an oil-immersed polypropylene film for electrical insulation, characterized in that the oil content is 0%, and a method for producing the same.

本発明においてポリプロピレン層(1)を構成するポリ
プロピレンは、膨潤率を小さくするために、アイソタク
チックインデックス(II)が97%以上のものを用い
るのが好ましい。より好ましくは99%以上である。ま
た、該PPの極限粘度[η]が1.4〜2.3であると
油への溶出弁が減少するばかりか、製膜製も良好となり
、この結果、機械特性、絶縁破壊電圧が良好となるので
好ましい。
In the present invention, the polypropylene constituting the polypropylene layer (1) preferably has an isotactic index (II) of 97% or more in order to reduce the swelling ratio. More preferably, it is 99% or more. In addition, when the intrinsic viscosity [η] of the PP is 1.4 to 2.3, not only the elution valve into oil is reduced, but also the film formation is good, and as a result, mechanical properties and dielectric breakdown voltage are good. This is preferable.

ざら、に該PPI!f(I)は、配向していると、絶縁
破壊電圧、機械特性、膨潤特性いずれも良好となるので
好ましく、−軸配向の場合、複屈折が0゜015〜0.
035の範囲、二軸配向の場合、面配向が0.010−
0.020の範囲のものが上記観点から好ましい。
Zara, the PPI! When f(I) is oriented, dielectric breakdown voltage, mechanical properties, and swelling properties are all improved, so it is preferable, and when it is -axis oriented, the birefringence is 0°015 to 0.0°.
035 range, in the case of biaxial orientation, the plane orientation is 0.010-
A value in the range of 0.020 is preferable from the above viewpoint.

さらに、PP層(1)は、実質的に空孔を含有していな
いことが必要である。本発明において実質的にとは、例
えば、ポリプロピレン延伸等により付随的に生ずる微傷
な空孔の含有は許される。
Furthermore, the PP layer (1) needs to be substantially free of pores. In the present invention, "substantially" means, for example, that the inclusion of slight pores incidentally caused by polypropylene stretching or the like is allowed.

しかしながら、絶縁破壊電圧を良好とする上で、このよ
うな空孔は極力含有していないことが好ましく、この観
点から該空孔の含有率は、5%未満であることが好まし
い。
However, in order to improve the dielectric breakdown voltage, it is preferable to contain as few such pores as possible, and from this point of view, it is preferable that the pore content is less than 5%.

次に多孔質ポリプロピレン層(H)とは、空孔率が30
〜85%であることが必要であり、好ましくは、40〜
80%である。空孔率が、小さすぎると、絶縁油に浸漬
した際の膨潤率が増大するばかりか、絶縁油の流動性が
低下し部分発熱し絶縁破壊の原因となる。一方、空孔率
が大きすぎると、(H>層がへき開し易くなり、特にケ
ーブルの様に大ぎな力が加わる場合(H)層が剥離して
絶縁破壊の原因となる。
Next, the porous polypropylene layer (H) has a porosity of 30
It is necessary that it is ~85%, preferably 40~85%.
It is 80%. If the porosity is too small, not only will the swelling rate increase when immersed in insulating oil, but the fluidity of the insulating oil will decrease, causing partial heat generation and dielectric breakdown. On the other hand, if the porosity is too large, the (H) layer is likely to cleave, and especially when a large force is applied, such as in a cable, the (H) layer will peel off, causing dielectric breakdown.

また、該多孔質PP層(H)の平均孔径は、0゜01〜
5μmでおることが必要であり、好ましくは、0.1〜
3μmである。平均孔径が小さすぎると、絶縁油の含浸
性、流動性に劣ると同時に、油による膨潤率も増大し絶
縁破壊の原因となる。
Moreover, the average pore diameter of the porous PP layer (H) is 0°01~
It is necessary to have a thickness of 5 μm, preferably 0.1 to 5 μm.
It is 3 μm. If the average pore diameter is too small, impregnating properties and fluidity with insulating oil will be poor, and at the same time, the swelling rate due to oil will increase, causing dielectric breakdown.

一方、平均孔径が大きすぎると、絶縁破壊電圧が低下す
る等の絶縁欠陥の原因となる。
On the other hand, if the average pore diameter is too large, it causes insulation defects such as a decrease in dielectric breakdown voltage.

また、(H)層の機械強度を高める上で、該PPの[η
]は1.6〜3.0dl/gであることが好ましい。ま
た、IIが96%以上であると、絶縁油に対する溶解度
が低下するので好ましい。
In addition, in increasing the mechanical strength of the (H) layer, the [η
] is preferably 1.6 to 3.0 dl/g. Further, it is preferable that II is 96% or more because the solubility in insulating oil decreases.

ポリプロピレン層(I)と多孔質ポリプロピレン層(H
)との構成は、(I)/(H)あるいは(H)/ (1
)/ (H)であり、(I>層の全厚みに占める分率は
、50〜90%であり、好ましくは、60〜80%であ
る。
Polypropylene layer (I) and porous polypropylene layer (H
) is (I)/(H) or (H)/(1
)/(H), and the fraction of (I> in the total thickness of the layer is 50 to 90%, preferably 60 to 80%.

(I>層の厚み分率が小さすぎると、機械強度が低下す
るばかりか、絶縁破壊電圧が低下する。
(I> If the thickness fraction of the layer is too small, not only the mechanical strength will decrease, but also the dielectric breakdown voltage will decrease.

一方、厚み分率が大きすぎると、油含浸性及び膨潤特性
に劣り特にコロナ放電電圧が低下し破壊し易くなる。
On the other hand, if the thickness fraction is too large, the oil impregnating property and swelling properties will be poor, and in particular, the corona discharge voltage will decrease, making it easy to break.

本発明ポリプロピレンフィルムには、膨潤率をざらに低
下させる目的で、仝層もしくは、(I)層のみにエンボ
スを施しても良いが、絶縁破壊電圧を低下させない観点
からエンボス率は、50%以下であることが好ましい。
The polypropylene film of the present invention may be embossed on only one layer or the (I) layer in order to roughly reduce the swelling ratio, but from the viewpoint of not reducing the dielectric breakdown voltage, the embossment ratio should be 50% or less. It is preferable that

次に本発明ポリプロピレンフィルムの製造方法について
説明する。
Next, a method for manufacturing the polypropylene film of the present invention will be explained.

本発明において、(H)層の原料としてポリプロピレン
に添加されるポリプロピレン以外の抽出可能な有機固体
とは、軟化点が35〜100℃、分子量が200〜10
00のものが好ましく、具体的には、ジシクロヘキシル
フタレート(D CHP)、トリフェニレンホスフェイ
ト(TPP)、セチルパルミエート、ステアリルスアレ
ート、バンタエリスリトールステアレートなどであり、
特に分子構造中に分極性及び極性基を含有するDCHP
、TPPが目的とする空孔率及び平均孔径を得る上で好
ましい。
In the present invention, the extractable organic solid other than polypropylene added to polypropylene as a raw material for the (H) layer has a softening point of 35 to 100°C and a molecular weight of 200 to 10°C.
00 is preferred, and specific examples include dicyclohexyl phthalate (D CHP), triphenylene phosphate (TPP), cetyl palmate, stearyl suarate, vantaerythritol stearate, etc.
Especially DCHP containing polarizable and polar groups in its molecular structure.
, TPP is preferred in terms of obtaining the desired porosity and average pore diameter.

本発明に於いては、上述の有機固体がポリプロピレン1
00重量部に対し、70〜180重量部であることが必
要であり、好ましくは、90〜160重量部である。添
加量が少なすぎると、形成される孔の空孔率、孔径共に
小さいものしか得られず、絶縁油の含浸性、膨潤特性共
に劣り絶縁破壊しやすくなる。一方、添加量が多すぎる
と、(H)層の押出し時に、該組成物の粘度が著しく低
下し押出しが困難になるばかりか、(1)層への有機固
体の移行量が増大して、この結果製造されたポリプロピ
レンフィルムの絶縁破壊電圧が低下する等の問題を生じ
る。
In the present invention, the above-mentioned organic solid is polypropylene 1
00 parts by weight, it is necessary to be 70 to 180 parts by weight, preferably 90 to 160 parts by weight. If the amount added is too small, the porosity and diameter of the pores formed will be small, and the impregnating properties and swelling properties of the insulating oil will be poor, resulting in easy dielectric breakdown. On the other hand, if the amount added is too large, not only will the viscosity of the composition significantly decrease and extrusion become difficult when extruding the (H) layer, but also the amount of organic solid transferred to the (1) layer will increase. As a result, problems such as a decrease in dielectric breakdown voltage of the produced polypropylene film arise.

本発明においては、(I)層を形成するポリプロピレン
樹脂及び(H)層を形成するポリプロピレンと有機固体
からなる組成物とを別々の押出機より溶融押出し、一つ
の口金内で積層して、(1)/(H)あるいは、(H)
/ (I)/ (H)からなる構成のシートあるいはチ
ューブ状に形成し押出す。ここで口金内で積層するとは
、口金より押出された際にはすでに積層体として形成さ
れていることを意味し、具体的には、該積層方法として
押出機よりポリマーを口金に導く短管内で積層する方法
、及び、ロ金内マニホールド部で積層する方法が挙げら
れるが、特に有機固体の(1−1)層から(I)層への
移行を考慮するとマニホールド部で積層する方法が好ま
しい。また、積層方法としては、(I)層のみを形成し
ておき、未延伸あるいは少なくとも1軸に延伸した後に
別の押出機及び口金を使用して(ト1)層を形成する技
術も適応しjqる。しかし有機固体を多量に含有した(
H)と(I)層を強く接着、強固に一体化させるために
は前者の方法が優れている。
In the present invention, a composition consisting of a polypropylene resin forming the layer (I) and a polypropylene and an organic solid forming the layer (H) are melt-extruded from separate extruders, and laminated in one die. 1)/(H) or (H)
/ (I) / (H) Formed into a sheet or tube shape and extruded. Here, the term "laminated in the die" means that the polymer is already formed as a laminate when it is extruded from the die. Specifically, the lamination method is such that the polymer is laminated in a short tube that leads from the extruder to the die. Examples include a method of laminating layers and a method of laminating layers in a manifold section within the metal, but a method of layering layers in a manifold section is particularly preferable in consideration of the transition from the layer (1-1) of the organic solid to the layer (I). In addition, as a lamination method, a technique is applicable in which only the (I) layer is formed, and after unstretched or at least uniaxially stretched, a separate extruder and die are used to form the (T1) layer. I want to do it. However, it contained a large amount of organic solids (
The former method is superior for strongly adhering and solidly integrating layers H) and (I).

以上の様に押出されたシートあるいはチューブ状物は、
冷却ドラムあるいは冷却マンドレル、水槽等で冷却した
後に、抽出層に導き有機固体を抽出する、該有機固体の
場合、ポリプロピレンを溶出しない有効な抽出溶媒とし
ては、トリクロルエチレン、トリクロルメタン、メチル
エチルケトン、トルエン、キシレン、メタノール、酢酸
エチル等が挙げられる。
The sheet or tube-shaped product extruded as described above is
After cooling with a cooling drum, cooling mandrel, water tank, etc., the organic solid is introduced into an extraction layer and extracted. In the case of the organic solid, effective extraction solvents that do not elute polypropylene include trichlorethylene, trichloromethane, methyl ethyl ketone, toluene, Examples include xylene, methanol, and ethyl acetate.

また、本発明においては、抽出前あるいは、抽出後又は
抽出中に、延伸を行っても良く、さらに、部分的に有機
固体を抽出しておき、延伸を行なった後、完全に有機固
体を抽出する方法でも良いが、延伸工程では、添加して
いる物質の移動が層間で生じ易く、この観点から、延伸
前に少なくとも添加している有機固体の一部、好ましく
は、30%以上を抽出しておくことが好ましい。
Furthermore, in the present invention, stretching may be performed before, after, or during extraction, and furthermore, organic solids may be partially extracted, and after stretching, organic solids may be completely extracted. However, in the stretching process, the added substances tend to migrate between layers, and from this point of view, at least a part, preferably 30% or more, of the added organic solids is extracted before stretching. It is preferable to keep it.

また、延伸時の延伸倍率は一軸方向について、2〜15
倍、2軸延伸する場合は、面倍率で5〜48倍の範囲で
あるとフィルムの平面性、機械特性、絶縁破壊電圧いず
れも良好となるので好ましい。
In addition, the stretching ratio during stretching is 2 to 15 in the uniaxial direction.
In the case of double or biaxial stretching, it is preferable that the areal magnification is in the range of 5 to 48 times because the flatness, mechanical properties, and dielectric breakdown voltage of the film are all good.

上記工程の俊、完全に有機固体が抽出された状態で、1
20〜170℃の温度で熱処理して本発明フィルムを得
る。
In the above step, with the organic solids completely extracted, 1
The film of the present invention is obtained by heat treatment at a temperature of 20 to 170°C.

本発明は、以上に述べたような特性を持つことを特徴と
するものであるが、このフィルムの長手方向の熱収縮率
が0.5〜6%、好ましくは1〜4%の範囲にあると、
油浸時の寸法変化が小さくなり、素子の巻締り、しわの
発生がなくなり長期信頼性が向上するので好ましい。
The present invention is characterized by having the properties described above, and the heat shrinkage rate of this film in the longitudinal direction is in the range of 0.5 to 6%, preferably 1 to 4%. and,
This is preferable because the dimensional change during oil immersion is reduced, the winding tightening of the element and the occurrence of wrinkles are eliminated, and long-term reliability is improved.

[作用] 本発明は、ポリプロピレン層(I)の少なくとも片面に
平均孔径が0.01〜5μm、空孔率を20〜80%と
した多孔質ポリプロピレン層(H>を積層したことによ
り油含浸性を良好とし、しかも、油による膨潤を抑制で
きたものである。
[Function] The present invention has a porous polypropylene layer (H>) having an average pore diameter of 0.01 to 5 μm and a porosity of 20 to 80% on at least one side of the polypropylene layer (I), thereby improving oil impregnability. In addition, it was possible to suppress swelling due to oil.

[特性の測定方法並びに効果の評価方法1次に本発明に
ついての測定方法及び評価方法について、まとめて示す
[Method of Measuring Characteristics and Method of Evaluating Effects 1] Next, the measuring methods and evaluation methods of the present invention will be summarized.

(1)  アイソタクチックインデックス(I I>試
料を130℃で2時間真空乾燥する。これから重ffi
W(m(J)の試料をとり、ソックスレー抽出器に入れ
、沸111j!n−へブタンで12時間抽出する。
(1) Isotactic index (II) Vacuum dry the sample at 130°C for 2 hours.
A sample of W(m(J)) is taken, placed in a Soxhlet extractor, and extracted with boiling 111j!n-hebutane for 12 hours.

次に、この試料を取出し、アセトンで十分洗浄した後、
130℃で6時間真空乾燥し、その後手ff1W’  
(mO)を測定し、次式で求める。
Next, take out this sample, wash it thoroughly with acetone, and then
Vacuum dry at 130°C for 6 hours, then hand ff1W'
(mO) is measured and calculated using the following formula.

II(%)= (W’ /W)xloo(2)極限粘度
([η]) ASTM  D  1601に従って、試料0.10を
135℃のテトラリン100m1に完全溶解させ、測定
したもので、旧/gで表す。
II (%) = (W' /W) Expressed as

(3)  平均孔径 走査型電子顕微鏡(SEM)による表面および断面観察
結果から求めた。
(3) Average pore diameter Determined from surface and cross-sectional observation results using a scanning electron microscope (SEM).

(4)空孔率(Pr) 試料(10cmx 10cm)を流動パラフィンに24
時間浸漬し、表層の流動パラフィンを十分に拭きとった
後の重量(W2)を測定し、該試料の浸漬前の重量(W
l)流動パラフィンの密度(ρ)より空孔体積(vO)
を次式で求める。
(4) Porosity (Pr) Sample (10cm x 10cm) was soaked in liquid paraffin for 24 hours.
The weight (W2) after immersing the sample for an hour and thoroughly wiping off the liquid paraffin on the surface layer was measured, and the weight (W2) of the sample before immersion was measured.
l) Pore volume (vO) from density (ρ) of liquid paraffin
is calculated using the following formula.

Vo = (W2−Wl)/ρ 空孔率(Pr)は、全層の見掛は体1(厚み、寸法より
計算される値)■、空孔体積Vo及びポリプロピレン層
(1)の体積(Vl)を用いて次式で求める。
Vo = (W2-Wl)/ρ The porosity (Pr) is the apparent volume of the entire layer (value calculated from the thickness and dimensions), the pore volume Vo, and the volume of the polypropylene layer (1) ( Vl) using the following formula.

Pr=Vo / (V−Vl)xloo (%)(5)
  複屈折 アツベの屈折計を用いて、フィルムの長手方向の屈折率
(Ny>及び幅方向の屈折率(NX)を測定し、Nyと
NXとの差の絶対値を複屈折とする。尚、測定時の光源
にはナトリウムD線を用い、マウント液としては、サリ
チル酸メチルを用いる。
Pr=Vo/(V-Vl)xloo (%) (5)
Birefringence Using Atsube's refractometer, measure the refractive index in the longitudinal direction (Ny>) and the refractive index in the width direction (NX) of the film, and take the absolute value of the difference between Ny and NX as birefringence. A sodium D line is used as a light source during measurement, and methyl salicylate is used as a mounting liquid.

(6)  面配向 アラへの屈折計を用いて、フィルムの長手方向、幅方向
、厚み方向のそれぞれの屈折率、Ny、NX、NZを測
定し、次式で求める。
(6) Using a refractometer for plane orientation, measure the refractive index, Ny, NX, and NZ in the longitudinal direction, width direction, and thickness direction of the film, and calculate them using the following equations.

面配向= (Ny+Nx>/2−Nz 尚、測定条件は複屈折と同様である。Planar orientation = (Ny+Nx>/2-Nz Note that the measurement conditions are the same as for birefringence.

(7)  熱収縮率 フィルムから、長さ200mm、幅1101I1の試料
を切取る(熱収縮率を測定する方向を長さ方向とする)
。この試料を120℃の熱風循環オーブン中に15分間
保持した後、室温中に取出し、その長さL(mm>を測
定し、次式で求める。
(7) Cut a sample with a length of 200 mm and a width of 1101I1 from the heat shrinkage film (the direction in which the heat shrinkage is measured is the length direction).
. After holding this sample in a hot air circulation oven at 120° C. for 15 minutes, it is taken out to room temperature, and its length L (mm>) is measured and determined by the following formula.

熱収縮率(%) =100 X (200−L ) /
200(8)  絶縁油による膨潤度 フィルムから、30mmx 30mmの試料を切取り、
厚み(Dl)を測定する。次にこの試料を100℃のア
ルキルベンゼン油中に浸し、1kC1/mm2の荷重下
で24時間油浸後、室温まで冷却し直ちにこの試料を取
出し厚み(D2)を測定する。
Heat shrinkage rate (%) = 100 x (200-L) /
200 (8) Degree of swelling with insulating oil Cut a sample of 30 mm x 30 mm from the film,
Measure the thickness (Dl). Next, this sample is immersed in alkylbenzene oil at 100°C, and after being immersed in the oil for 24 hours under a load of 1 kC1/mm2, the sample is cooled to room temperature, and the sample is immediately taken out and its thickness (D2) is measured.

膨潤度は、次式で計算される。The degree of swelling is calculated using the following formula.

膨潤度(%)=100X (D2−Dl)/D1(9)
  絶縁油の流通性 フィルムとアルミニウム箔とを交互巻きにして、コンデ
ンサー素子を作る。これを絶縁油中に浸して、油を真空
含浸せしめる。しかる後、素子を解体して、素子のあら
ゆる層間に、絶縁油がいきわたっているかどうかを肉眼
で判定する。
Swelling degree (%) = 100X (D2-Dl)/D1(9)
A capacitor element is made by alternately wrapping insulating oil circulation film and aluminum foil. This is immersed in insulating oil and vacuum impregnated with oil. Thereafter, the device is disassembled and visually determined whether the insulating oil has spread between all layers of the device.

ランクA:全面に均一にいきわたっている。Rank A: Evenly distributed over the entire surface.

ランクB:微かに油のない点が存在する。Rank B: There are slight oil-free spots.

ランクC:油のない部分が面状に存在する。Rank C: There is a planar portion without oil.

(10)  電気絶縁油 鉱油、ヒマシ油、アルキルベンゼン、ジアリルアルカン
、ポリブテン油、シリコン油など、各種公知の電気絶縁
油の総称である。
(10) Electrical insulating oil A general term for various known electrical insulating oils such as mineral oil, castor oil, alkylbenzene, diallylalkane, polybutene oil, and silicone oil.

[実施例] 次に実施例に基づき本発明を説明する。[Example] Next, the present invention will be explained based on examples.

実施例1及び2 PP層(1)として、IIが97%、[η]が1.8d
l/!:lのPP樹脂、多孔質PP層(H)の原料とし
て、IIが97%、[η]が2.3dl/gのPP樹脂
100重量部とシシクロヘキシルフタレ−ト(DCHP
、融点63℃)150重(5)部との組成物を用意しそ
れぞれ別の押出はを用いて溶融押出し、Tダイ内マニホ
ールド部で積層し、(I)層/(H)層からなるシート
押出した。かかるシートは、60℃の冷却ドラム上で冷
却固化し、直ちにトリクレンバス中に導き、(H)li
J中のDCHPを99.7%以上抽出した。
Examples 1 and 2 As the PP layer (1), II was 97% and [η] was 1.8d
l/! :1 PP resin, as raw materials for the porous PP layer (H), 100 parts by weight of PP resin with 97% II and 2.3 dl/g, and cyclohexyl phthalate (DCHP).
, melting point 63°C) and 150 parts by weight (5) were prepared and melt-extruded using separate extruders, and laminated in the manifold part of the T-die to form a sheet consisting of (I) layer/(H) layer. Extruded. Such a sheet was cooled and solidified on a cooling drum at 60°C, immediately introduced into a trichlene bath, and (H)li
More than 99.7% of DCHP in J was extracted.

こうして1qられたシートは、全厚みが700μmであ
り、(I)層が600μm、(ト1)層が100μmで
あった。次に該シートを140℃で予熱し長手方向(以
下MDと略称する)に7.5倍に延伸俊、150℃にて
MDに5%のリラックスを許しながら熱処理して巻き取
った(実施例1)。
The total thickness of the thus prepared 1q sheet was 700 μm, the (I) layer was 600 μm, and the (T1) layer was 100 μm. Next, the sheet was preheated at 140°C, stretched 7.5 times in the longitudinal direction (hereinafter abbreviated as MD), heat-treated at 150°C while allowing 5% relaxation in MD, and then rolled up (Example 1).

また、該シートを140℃にてMDに4.5倍延伸後、
ステンターに導き横方向(以下TDと略称する)に15
5℃にて9倍に延伸し、160℃にて7%のリラックス
を許しながら熱処理を行いエツジ部をスリット後巻きと
った(実施例2)以上の様にして得られたフィルムの特
性を評価したところ表1の様になり、いずれも、油含浸
性、膨潤特性に優れ油浸絶縁材料として極めて優れてい
ることが分る。
In addition, after stretching the sheet 4.5 times in the MD at 140°C,
15 in the lateral direction (hereinafter abbreviated as TD) into the stenter.
The film was stretched 9 times at 5°C, heat treated at 160°C while allowing 7% relaxation, and the edges were slit and then rolled up (Example 2) The properties of the film obtained as described above were evaluated. The result is as shown in Table 1, and it can be seen that all of them have excellent oil impregnation properties and swelling properties, and are extremely excellent as oil-immersed insulating materials.

比較例1及び2 市販の油浸コンデンザ用2軸延伸ポリプロピレンフィル
ムの平滑タイプ(比較例1)、及び片面粗面化タイプ(
比較例2)を入手し、評価を行った。この結果を実施例
と比較して、表1にまとめて示すが、比較例2では、油
含浸性を有しているものの、比較例1.2いずれも膨潤
度が大きく、油浸絶縁材料として問題があることがわか
る。
Comparative Examples 1 and 2 Commercially available biaxially oriented polypropylene films for oil-immersed condensers of a smooth type (Comparative Example 1) and a one-sided roughened type (
Comparative Example 2) was obtained and evaluated. The results are compared with Examples and summarized in Table 1. Although Comparative Example 2 has oil-impregnated properties, both Comparative Examples 1 and 2 have a large degree of swelling and can be used as oil-impregnated insulating materials. I can see there is a problem.

実施例3 PP層(I)として、IIが99.2%、[η]が2.
1dl/aのPP樹脂、多孔質PP層(H)として、I
Iが99%、[ηコが2.5d110のPP樹樹脂10
型 (TPP、融点49℃)140重間部との組成物をそれ
ぞれ別の押出機を用いて溶融押出し、(H)/(I)/
(H)3層からなるシートを口金内で積層して押出し、
70℃の冷却ドラム上で冷却固化し、実施例2と同様に
して抽出後、4.2層9倍(HDxTD)の2軸延伸、
熱固定を行い厚さ50μmのフィルムを得た。かかるフ
ィルムの特性を表1にまとめて示すが、実施例1、2同
様、油含浸性、膨潤特性共に良好であることが分る。
Example 3 As the PP layer (I), II was 99.2% and [η] was 2.
1 dl/a PP resin, as a porous PP layer (H), I
PP resin 10 with 99% I and 2.5d110
(H)/(I)/
(H) A sheet consisting of three layers is laminated and extruded in a nozzle,
Cooled and solidified on a cooling drum at 70°C, extracted in the same manner as in Example 2, and then biaxially stretched with 4.2 layers and 9 times (HD x TD).
Heat setting was performed to obtain a film with a thickness of 50 μm. The properties of this film are summarized in Table 1, and it can be seen that, like Examples 1 and 2, both oil impregnation and swelling properties are good.

比較例3 (H)層の原料として、IIが97%、[η]が1.8
dl/aのPP樹脂と炭酸カルシウム(金平炭カル製、
平均粒径3μm)25重量部との組成物を用いた以外は
実施例3と同様にして溶融押出し、溶融シート冷却後、
2軸延伸しフィルムを得た。かかるフィルムの特性を評
価した結果を表1にまとめて示すが、(H>層の平均孔
径は30μmと大きいために、絶縁油に対する濡れ性に
劣り、絶縁油の流通性はランクCであり、油浸絶縁材料
としては使用できないことが分る。
Comparative Example 3 As a raw material for the (H) layer, II was 97% and [η] was 1.8.
dl/a PP resin and calcium carbonate (manufactured by Kinpei Tancal,
After melt extrusion and cooling of the melt sheet in the same manner as in Example 3 except for using a composition with 25 parts by weight (average particle size 3 μm),
A biaxially stretched film was obtained. The results of evaluating the properties of such a film are summarized in Table 1. (H> Because the average pore diameter of the layer is as large as 30 μm, the wettability to insulating oil is poor, and the flowability of insulating oil is rank C. It turns out that it cannot be used as an oil-immersed insulating material.

実施例4 PP層(I)及び多孔質PP層(H)として実施例1と
同じ原料を用意し、今度は(I)層原料のみを押出機よ
り、Tダイより単層で押出し、50℃の冷却ドラム上で
冷却し、引続き140℃にて4.2倍にMDに延伸した
。かかる−軸延伸フィルムをステンターに導く前に、多
孔質PP層原料を別な押出機より押出し該−軸延伸フィ
ルムの片面に積層し、150℃にてTDに9倍延伸しエ
ツジ部スリット俊巻きとった。
Example 4 The same raw materials as in Example 1 were prepared for the PP layer (I) and the porous PP layer (H), and this time only the raw material for the (I) layer was extruded as a single layer from a T-die using an extruder at 50°C. The film was cooled on a cooling drum, and then stretched to 4.2 times in the MD at 140°C. Before introducing the axially stretched film into a stenter, the raw material for the porous PP layer is extruded from a separate extruder, laminated on one side of the axially stretched film, stretched 9 times in the TD at 150°C, and slitted at the edges. I took it.

次にかかる2軸延伸フイルムを実施例1と同様にしてト
リクレンバス中に導き、(H>層中のDCHPを99.
7%以上抽出した後、120’Cで乾燥後、155℃で
緊張熱処理をした後巻きとった。
Next, the biaxially stretched film was introduced into a Triclean bath in the same manner as in Example 1, and the DCHP in the layer was set to 99.
After extracting 7% or more, it was dried at 120'C, subjected to tension heat treatment at 155C, and then rolled up.

かかるフィルムの構成及び特性をまとめて表1に示すが
、膨潤度、絶縁油の流通性ともに優れた特性を有してい
ることが分る。
The structure and properties of this film are summarized in Table 1, and it can be seen that the film has excellent properties in both swelling degree and insulating oil distribution.

[発明の効果] かくして1qられた本発明の油浸電気絶縁用ポリプロピ
レンフィルム及びその製造方法は、次のような効果を奏
するものである。
[Effects of the Invention] The oil-immersed polypropylene film for electrical insulation of the present invention thus obtained and the method for producing the same have the following effects.

(1)  絶縁油の含浸性・流動性に優れ素子を油浸素
子を形成した際の初期特性が安定している。
(1) Excellent insulating oil impregnability and fluidity, and stable initial characteristics when an oil-immersed element is formed.

(2)  絶縁油浸漬時の膨潤率が極めて小さいために
素子内圧が上昇する等のトラブルがなく長期信頼性が高
い。
(2) Since the swelling rate when immersed in insulating oil is extremely small, there are no problems such as increases in internal pressure of the element, and long-term reliability is high.

(3)  表層に形成されている多孔質層の均一性が極
めて高いために特にコロナ破壊電圧が高い。
(3) Since the porous layer formed on the surface layer has extremely high uniformity, the corona breakdown voltage is particularly high.

従って、コンデンサ、ケーブル、トランス、モーター、
ジェネレータ等の油浸電気機器等の絶縁層として好適な
ものであり、特に、油浸コンデンサにおいては、電極を
アルミニウム、亜鉛等の金属蒸着により形成するタイプ
では、本発明フィルムの多孔質ポリプロピレン層側に該
蒸着層を形成してやると該層の油浸時の寸法変化が極め
て小さいため、該蒸着層に亀裂が入りコンデサのtan
δが増大する等の問題が避けられ好ましい。
Therefore, capacitors, cables, transformers, motors,
It is suitable as an insulating layer for oil-immersed electrical equipment such as generators, etc. In particular, in oil-immersed capacitors, the porous polypropylene layer side of the film of the present invention is of a type in which electrodes are formed by vapor deposition of metals such as aluminum and zinc. When the vapor deposited layer is formed, the dimensional change of the layer when immersed in oil is extremely small, so cracks occur in the vapor deposited layer and the tan of the capacitor increases.
This is preferable because problems such as an increase in δ can be avoided.

Claims (3)

【特許請求の範囲】[Claims] (1)実質的に空孔を含有しないポリプロピレン層(I
)の少なくとも片面に空孔率が30〜85%、平均孔径
が0.01〜5μmである多孔質ポリプロピレン層(H
)が積層され、かつ(I)層の厚み分率が50〜90%
であることを特徴とする油浸電気絶縁用ポリプロピレン
フイルム。
(1) Polypropylene layer containing substantially no pores (I
) with a porous polypropylene layer (H
) are laminated, and the thickness fraction of the (I) layer is 50 to 90%.
An oil-immersed polypropylene film for electrical insulation.
(2)ポリプロピレン100重量部と、ポリプロピレン
以外の抽出可能な有機固体70〜180重量部からなる
組成物(イ)とポリプロピレン樹脂(ロ)とをそれぞれ
別の押出し機を用い溶融押出し口金内で積層し、溶融形
成した後に、該有機固体を抽出することを特徴とする特
許請求の範囲第1項の油浸電気絶縁用ポリプロピレンフ
イルムの製造方法。
(2) Composition (a) consisting of 100 parts by weight of polypropylene and 70 to 180 parts by weight of extractable organic solids other than polypropylene and polypropylene resin (b) are laminated in a melt extrusion die using separate extruders. The method for producing an oil-immersed polypropylene film for electrical insulation according to claim 1, characterized in that the organic solid is extracted after the melt formation.
(3)抽出可能な有機固体がジシクロヘキシルフタレー
トとトリフェニレンフォスフェイトから選ばれた少なく
とも一種であることを特徴とする特許請求の範囲第2項
に記載の油浸電気絶縁用ポリプロピレンフイルムの製造
方法。
(3) The method for producing an oil-immersed polypropylene film for electrical insulation according to claim 2, wherein the extractable organic solid is at least one selected from dicyclohexyl phthalate and triphenylene phosphate.
JP5458187A 1987-03-10 1987-03-10 Oil-immersed polypropylene film for electrical insulation and method for producing the same Expired - Lifetime JPH074899B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5458187A JPH074899B2 (en) 1987-03-10 1987-03-10 Oil-immersed polypropylene film for electrical insulation and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5458187A JPH074899B2 (en) 1987-03-10 1987-03-10 Oil-immersed polypropylene film for electrical insulation and method for producing the same

Publications (2)

Publication Number Publication Date
JPS63221037A true JPS63221037A (en) 1988-09-14
JPH074899B2 JPH074899B2 (en) 1995-01-25

Family

ID=12974664

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH074899B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014077325A1 (en) * 2012-11-19 2014-05-22 日東電工株式会社 Electrically insulating resin sheet for motor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014077325A1 (en) * 2012-11-19 2014-05-22 日東電工株式会社 Electrically insulating resin sheet for motor
JP2014102946A (en) * 2012-11-19 2014-06-05 Nitto Denko Corp Electrically-insulating resin sheet for motor

Also Published As

Publication number Publication date
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