JPH0531781A - Thermoplastic polyimide-based tubular film - Google Patents

Thermoplastic polyimide-based tubular film

Info

Publication number
JPH0531781A
JPH0531781A JP3280947A JP28094791A JPH0531781A JP H0531781 A JPH0531781 A JP H0531781A JP 3280947 A JP3280947 A JP 3280947A JP 28094791 A JP28094791 A JP 28094791A JP H0531781 A JPH0531781 A JP H0531781A
Authority
JP
Japan
Prior art keywords
film
thermoplastic polyimide
melt
tubular film
polyimide
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
JP3280947A
Other languages
Japanese (ja)
Other versions
JP3237715B2 (en
Inventor
Akihiro Tanaka
章博 田中
Tatsuro Kitaura
達郎 北浦
Junya Kanetake
潤也 金武
Tsutomu Yoshida
勉 吉田
Satoshi Wakinaka
敏 脇中
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.)
Gunze Ltd
Original Assignee
Gunze 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 Gunze Ltd filed Critical Gunze Ltd
Priority to JP28094791A priority Critical patent/JP3237715B2/en
Publication of JPH0531781A publication Critical patent/JPH0531781A/en
Priority to US08/232,312 priority patent/US5389412A/en
Priority claimed from US08/232,312 external-priority patent/US5389412A/en
Application granted granted Critical
Publication of JP3237715B2 publication Critical patent/JP3237715B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To provide thermoplastic polyimide-based tubular film, which is produced by melt-extruding material mainly made of brand-new type thermoplastic polyimide-based resin different from the conventional polyimide-based resin in the form of film. CONSTITUTION:Polyimide-based resin with water content of 30 ppm or less is melt-extruded in the form of tube with an extruder, the inner surface of the cylinder of which is lined by special alloy and at the tip of the cylinder and near the head of which filters are arranged. Next, after being cooled by cooling system with a water tank, the resultant tubular resin is stretched and heat-set. By being turned into film as described above, thermoplastic polyimide- based tubular film having excellent dimensional accuracy and film thickness accuracy is obtained, resulting in expecting to be used in wide field.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は溶融押出成膜されてなる
熱可塑性ポリイミド系チューブ状フィルムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a thermoplastic polyimide tubular film formed by melt extrusion film formation.

【0002】[0002]

【従来の技術】従来より、ポリイミド系フィルムは耐熱
性フィルムとして各種の用途に使用されているが、この
ポリイミド系フィルムは主としてポリイミドの前駆体で
あるポリイミド酸の溶液から流延法(キャスト法)によ
り薄膜を作り、その後乾燥・脱水・閉環させてフィルム
を成膜するのが一般的であった。
2. Description of the Related Art Conventionally, a polyimide film has been used as a heat-resistant film for various purposes. This polyimide film is mainly cast from a solution of a polyimide acid, which is a precursor of polyimide. It was general that a thin film was formed by the method described above, and then the film was formed by drying, dehydration and ring closure.

【0003】[0003]

【発明が解決しょうとする課題】流延法により成膜され
たポリイミド系フィルムは製造の際生産性が劣り、溶剤
を使用するために環境汚染や衛生上にも問題があり、し
かも高価格なものであった。
[Problems to be Solved by the Invention] The polyimide film formed by the casting method has a poor productivity in the production, and since it uses a solvent, it has problems in environmental pollution and hygiene, and is expensive. It was a thing.

【0004】本発明者らは上記の課題を解決するため
に、熱可塑性ポリイミド系樹脂を主成分とした素材を用
いて溶融押出法により極めて高い寸法精度と膜厚精度の
チューブ状フィルムを得るべく種々研究を重ねてついに
本発明に到達した。
In order to solve the above problems, the present inventors have aimed to obtain a tubular film with extremely high dimensional accuracy and film thickness accuracy by a melt extrusion method using a material whose main component is a thermoplastic polyimide resin. Through various studies, the present invention was finally reached.

【0005】[0005]

【課題を解決するための手段】本発明は熱可塑性ポリイ
ミド系樹脂を主成分とし溶融押出成膜された寸法精度,
膜厚精度が優れた熱可塑性ポリイミド系チューブ状フィ
ルムに関する。
Means for Solving the Problems The present invention is based on a dimensional accuracy obtained by melt extrusion film formation using a thermoplastic polyimide resin as a main component.
The present invention relates to a thermoplastic polyimide-based tubular film having excellent film thickness accuracy.

【0006】本発明に係る熱可塑性ポリイミド系樹脂と
しては、従来の熱硬化型、または非熱硬化型イミド型樹
脂のいずれとも異なる全く新しいタイプの熱可塑性ポリ
イミド系樹脂である。このような樹脂としては、例えば
高化式フローテスター(ダイ10mm×0.1mm,予
熱時間5min)を用いて融点付近の380〜420℃
で測定した溶融粘度が1,000〜4,000ポイズの
ものを例示できる。斯かる溶融粘度の低い熱可塑性ポリ
イミド系樹脂を用いて溶融押出成膜するために、優れた
寸法精度、膜厚精度を有する熱可塑性ポリイミド系チュ
ーブ状フィルムを容易に成膜出来る。この際、溶融粘度
が上記範囲以外の熱可塑性ポリイミド系樹脂を溶融押出
成膜してもよいが、寸法精度、膜厚精度が低下する傾向
になり好ましくない場合が多く、また成膜も困難である
場合が多い。しかしながら、溶融粘度が上記範囲以外の
熱可塑性ポリイミド系樹脂も用途によっては使用可能で
あり、必ずしも上記の範囲のみに限定されない。
The thermoplastic polyimide-based resin according to the present invention is a completely new type of thermoplastic polyimide-based resin which is different from the conventional thermosetting or non-thermosetting imide type resin. As such a resin, for example, using a Koka type flow tester (die 10 mm × 0.1 mm, preheating time 5 min), a melting point near 380 to 420 ° C.
The melt viscosity measured in 1. can be 1,000 to 4,000 poise. Since such a melt-extruded film is formed using a thermoplastic polyimide resin having a low melt viscosity, a thermoplastic polyimide tube film having excellent dimensional accuracy and film thickness accuracy can be easily formed. At this time, a melt extrusion film of a thermoplastic polyimide resin having a melt viscosity other than the above range may be melt-extruded into a film, but the dimensional accuracy and the film thickness accuracy tend to be deteriorated in many cases, and the film formation is also difficult. Often there is. However, a thermoplastic polyimide resin having a melt viscosity outside the above range can be used depending on the application, and is not necessarily limited to the above range.

【0007】本発明の熱可塑性ポリイミド系樹脂は単独
で溶融押出成膜してもよいが、熱伝導性を向上させるた
めに無機系充填剤を混合してもさしつかえなく、このこ
とに特に制限はない。この際、斯る無機系充填剤として
は、導電性カーボン、タルク、チタン酸フィスカー、チ
ッ化ボロン等を例示できるが、これのみに制限されな
い。又、熱可塑性ポリイミド系樹脂の性能を著しく低下
させないならば安定剤、滑剤、界面活性剤、顔料、ポリ
イミド系樹脂以外の樹脂等を添加してもよく、このこと
は特に制限されない。
The thermoplastic polyimide resin of the present invention may be melt-extruded and formed into a film by itself, but it may be mixed with an inorganic filler in order to improve thermal conductivity, and there is no particular limitation to this. Absent. At this time, examples of such an inorganic filler include conductive carbon, talc, fisker titanate, boron nitride, and the like, but are not limited thereto. Further, a stabilizer, a lubricant, a surfactant, a pigment, a resin other than the polyimide resin, etc. may be added as long as the performance of the thermoplastic polyimide resin is not significantly deteriorated, and this is not particularly limited.

【0008】本発明に係る熱可塑性ポリイミド系樹脂は
押出機に供給する際に水分含有量が30ppm以下にな
るように除湿乾燥する事が好ましく、水分含有量が30
ppm以上になるとポリイミト系樹脂が分解しやすく、
熱可塑流動性が悪化し、フイルムに気泡等が発生する現
象等によって、寸法精度、膜厚精度が優れた熱可塑性ポ
リイミド系チューブ状フィルムを成膜できない場合が多
く好ましくないケースもある。勿論、水分含有量が30
ppm以上の状態で押出機に供給してもいっこうに差し
つかえない。
The thermoplastic polyimide resin according to the present invention is preferably dehumidified and dried so that the water content is 30 ppm or less when it is supplied to the extruder.
If it is more than ppm, the polyimito resin will easily decompose,
In many cases, a thermoplastic polyimide-based tubular film having excellent dimensional accuracy and film thickness accuracy cannot be formed due to a phenomenon such as deterioration of thermoplastic fluidity and generation of bubbles in the film, which is not preferable. Of course, the water content is 30
Even if it is supplied to the extruder in the state of more than ppm, it will not be any problem.

【0009】本発明の熱可塑性ポリイミド系チューブ状
フィルムは一般的には環状ダイスを取付けた押出機を用
いて溶融押出でチューブ状に成膜されるが、この際、押
出機のシリンダーがチッ化鋼であると、チッ化鋼等が酸
化されてフィルムの中に金属酸化物が混入する場合が多
く、熱可塑性ポリイミド系フィルムの優れた性能を低下
させる傾向があり、チッ化鋼製のシリンダーを有する押
出機を使用するのは好ましくない場合が多い。しかし乍
ら必要ならばチッ化鋼製のシリンダーを使用してもよく
特に制限されない。
The thermoplastic polyimide-based tubular film of the present invention is generally formed into a tube by melt extrusion using an extruder equipped with an annular die. At this time, the cylinder of the extruder is nicked. In the case of steel, there are many cases where metal oxides are mixed in the film due to the oxidation of nitrogen nitride steel and the like, which tends to deteriorate the excellent performance of the thermoplastic polyimide film. It is often not preferred to use extruders that have them. However, if necessary, a cylinder made of nitrided steel may be used without any particular limitation.

【0010】本発明の熱可塑性ポリイミド系フィルムを
成膜するのに用いる押出機のシリンダーには、シリンダ
ーの内周面を特殊合金層で均一にライニングする事が好
ましく、斯る特殊合金層としては硬い耐食性合金マトリ
ックスの中にカーボン、マンガン、ケイ素、ボロン、ニ
ッケル、コバルト、クロム、タングステン、カーバイト
等一種もしくは二種以上が均一に分散されたライニング
材を例示できるが、必ずしもこれのみに限定されずチッ
化鋼の酸化を防止できるものであればこれ以外でもよ
い。
In the cylinder of the extruder used for forming the thermoplastic polyimide film of the present invention, it is preferable that the inner peripheral surface of the cylinder is uniformly lined with a special alloy layer. Carbon, manganese, silicon, boron, nickel, cobalt, chromium, tungsten, carbide and the like in a hard corrosion-resistant alloy matrix can be exemplified as a lining material in which one kind or two or more kinds are uniformly dispersed, but it is not always limited thereto. Other materials may be used as long as they can prevent the oxidation of the nitrided steel.

【0011】押出機に使用されるスクリューは急圧縮タ
イプが好ましくL/D=24〜29のものを例示できる
が、必ずしもこの値のみに限定されるものではない。
又、スクリューは硬質クロームメッキを施しておく事が
一般的であるが、このことも特に制限はない。
The screw used in the extruder is preferably a rapid compression type, and L / D = 24 to 29 can be exemplified, but the screw is not necessarily limited to this value.
Further, the screw is generally plated with hard chrome, but this is not particularly limited.

【0012】押出機の例えばシリンダー先端やヘッド付
近にはフィルムにゲル分子が混入するのを防止するため
に、必要ならば、ゲル濾過用フィルターを取り付けても
よい。 この際、斯る濾過用フィルターとしては、例え
ば繊維径の大なる金属繊維の不織布と繊維径の小なる金
属繊維の不織布とを積層したものをメッシュ状(例えば
ステンレス製)の保護層とメッシュ状(例えばステンレ
ス製)の支持層の間に挟み込み、しかる後燒結し一体化
に加工した度目5μ程度の目の細かいものが好ましい
が、この値は特に制限はない。このようなものとしては
リーフ型フィルターのものを例示するが、必ずしもこれ
のみに限定されず樹脂のゲル分子を濾過できるものであ
れば、これ以外でもよく特に制限はない。
If necessary, a filter for gel filtration may be attached to the tip of the cylinder or the vicinity of the head of the extruder in order to prevent gel molecules from being mixed in the film. At this time, as such a filter for filtration, for example, a laminate of a non-woven fabric of metal fibers having a large fiber diameter and a non-woven fabric of metal fibers having a small fiber diameter is used as a mesh-like protective layer and mesh-like one. It is preferable to use a fine mesh having a fineness of about 5 μ, which is sandwiched between (for example, stainless steel) support layers and then sintered and integrally processed, but this value is not particularly limited. Examples of such a filter include a leaf filter. However, the filter is not limited thereto, and any other filter may be used as long as it can filter gel molecules of the resin, and there is no particular limitation.

【0013】本発明の熱可塑性ポリイミド系チューブ状
フィルムを成膜するには上記の押出機に環状ダイスを取
付け、環状ダイスから押出されたチューブ状の内部に空
気等気体を吹き込み、所定の径(ダイスの押出径より小
さくてもよい)とした後冷却するインフレート法やデフ
レート法が好ましい。この際、環状ダイスは特に制限は
ないがスパイラルマンドレル方式のものが好ましいが、
これのみに限定されない。又、Tダイスを取付けてフラ
ット状フィルムに成膜してもよく特に制限はない。
To form the thermoplastic polyimide tubular film of the present invention, an annular die is attached to the above-mentioned extruder, and a gas such as air is blown into the tubular extruded from the annular die to give a predetermined diameter ( The inflating method or the deflate method in which the diameter is smaller than the extrusion diameter of the die) and then cooling is preferable. At this time, the circular die is not particularly limited, but a spiral mandrel type is preferable,
It is not limited to this. There is no particular limitation as long as a T-die is attached to form a film on a flat film.

【0014】冷却方法としては、特に限定されずインサ
イドマンドレル法、外部冷却法等適宣な方法を採用すれ
ば良いが、特に好ましい例としては真空水槽を例示でき
る。真空水槽とは真空ポンプ等により内部を減圧状態に
されたサイジングスリーブと冷却水槽とを有する構造で
あり、サイジングスリーブの内環表面即ちチューブと接
する面は平滑性の良好な材質(例えば鏡面仕上の施され
た金属やフッ素樹脂等)からなり、細孔が付設されてい
る。この細孔により常にチューブ状フィルムと接する面
が減圧状態となり、これによりチューブ状フィルムの外
径がスリーブ内環表面に沿って一定の径に規制される、
この際必要ならばスリーブの内環表面に少量の水等を供
給してスリーブ内環とチューブ状フィルム外表面との間
に薄い水膜を形成させてもよい。このような真空水槽に
よりチューブ状フィルムの外径が正確に規制されて冷却
されると共にその表面状態も良好なものになり寸法精度
は優れたものになる。
The cooling method is not particularly limited, and an appropriate method such as an inside mandrel method or an external cooling method may be adopted, and a particularly preferable example is a vacuum water tank. The vacuum water tank is a structure having a sizing sleeve and a cooling water tank whose inside is depressurized by a vacuum pump or the like, and the inner ring surface of the sizing sleeve, that is, the surface in contact with the tube is made of a material having good smoothness (for example, mirror finish). It is made of metal or fluororesin, etc., and has pores. Due to the pores, the surface in contact with the tubular film is in a reduced pressure state, whereby the outer diameter of the tubular film is regulated to a constant diameter along the sleeve inner ring surface,
At this time, if necessary, a small amount of water or the like may be supplied to the inner ring surface of the sleeve to form a thin water film between the inner ring of the sleeve and the outer surface of the tubular film. With such a vacuum water tank, the outer diameter of the tubular film is accurately regulated and cooled, and at the same time, the surface condition of the tubular film is improved and the dimensional accuracy is improved.

【0015】この際、前記冷却水槽は一般的なものでチ
ューブ状フィルム外表面が直接水と接している構造であ
っても、内部に冷却用媒体が出入りするジャケットを有
する直接水と接することのない環状構造であってもよく
特に制限はない。
At this time, even if the cooling water tank has a general structure in which the outer surface of the tubular film is in direct contact with water, it may be in direct contact with direct water having a jacket through which a cooling medium flows in and out. There is no particular limitation as long as it has no cyclic structure.

【0016】本発明に係る熱可塑性ポリイミド系チュー
ブ状フィルムは前述した押出機で成膜する際の押出条件
としては適宣に定めればよく特に制限されないが、具体
的には供給部310〜360℃、圧縮部360〜400
℃、溶融部370〜410℃、ダイス温度370〜41
0℃程度の値を例示できる。しかしながらこれらの値は
特に限定されない。スクリュウのスパイラル数は供給部
9〜15、圧縮部3〜8、溶融部7〜8を好適なものと
して例示できるが、この値は一例であって必ずしもこれ
のみに限定されない。
The thermoplastic polyimide-based tubular film according to the present invention is not particularly limited as long as it is appropriately set as the extrusion conditions for forming the film with the above-mentioned extruder, but specifically, the supply parts 310 to 360. C, compression part 360-400
℃, melting section 370-410 ℃, die temperature 370-41
A value of about 0 ° C. can be exemplified. However, these values are not particularly limited. As for the spiral number of the screw, the supply parts 9 to 15, the compression parts 3 to 8 and the melting parts 7 to 8 can be exemplified as suitable ones, but this value is an example and is not necessarily limited thereto.

【0017】本発明の熱可塑性ポリイミド系チューブ状
フィルムは高温での機械的強度等を向上させるために
は、2軸もしくは1軸に延伸し、更に必要ならばヒート
セットすることによって結晶化することが望ましい。結
晶化する際の結晶化度は特に制限しないが結晶化度10
〜35%にすることが好ましい。この場合、結晶化度が
10%以下になると200℃以上で熱変形が発生し好ま
しくない場合が多く、結晶化度35%以上になるともろ
くなりフィルムにクラックが発生し好ましくない場合が
多いが、用途によっては、かかる範囲以外の値のものも
使用可能である。この際、前記した延伸やヒートセット
を行なわなくても本発明の範囲であることは勿論であ
る。
The thermoplastic polyimide-based tubular film of the present invention should be biaxially or uniaxially stretched and crystallized by heat setting if necessary in order to improve mechanical strength at high temperature. Is desirable. The crystallinity at the time of crystallization is not particularly limited, but the crystallinity is 10
It is preferably set to ˜35%. In this case, if the crystallinity is 10% or less, thermal deformation often occurs at 200 ° C. or higher, which is not preferable, and if the crystallinity is 35% or higher, the film becomes brittle and cracks are generated in the film, which is not preferable. Depending on the application, a value outside this range can be used. At this time, it goes without saying that the scope of the present invention is not required to perform the above-mentioned stretching and heat setting.

【0018】延伸方法は特に制限はなく、適宜の方法で
実施すればよい。延伸条件は特に制限はないが、延伸温
度は250〜350℃、延伸倍率は1.2〜3倍が好ま
しく、延伸温度が250℃以下になると均一な延伸が困
難な傾向になり、350℃以上になると強度アップ等の
延伸効果が認められない場合が多く、また延伸倍率が
1.2倍以下になると結晶化が充分でなく強度、剛性率
の向上が期待できず、3倍以上に延伸すると膜厚精度が
低下しやすい傾向になり、延伸倍率は大きい程この膜厚
精度低下が著しく好ましくない場合が多い。勿論、これ
らの値はあくまでも一例であり、必要ならば上記の範囲
を越えても差し支えなく、特に制限を受けるものでな
い。
The stretching method is not particularly limited and may be any suitable method. The stretching conditions are not particularly limited, but the stretching temperature is preferably 250 to 350 ° C and the stretching ratio is preferably 1.2 to 3 times. When the stretching temperature is 250 ° C or less, uniform stretching tends to be difficult, and 350 ° C or more. In many cases, the stretching effect such as increase in strength is not recognized, and when the stretching ratio is 1.2 times or less, crystallization is not sufficient and improvement in strength and rigidity cannot be expected, and stretching is performed at 3 times or more. The accuracy of the film thickness tends to be lowered, and the higher the draw ratio is, the lower the accuracy of the film thickness is in many cases, which is not preferable. Of course, these values are merely examples, and the values may exceed the above range if necessary, and are not particularly limited.

【0019】必要に応じて行なわれるヒートセットは延
伸終了後そのままの状態で連続して行なう事が一般的で
あるが、これのみに限定されず、その他適宜な方法で行
なえばよい。ヒートセット温度は特に制限はないが30
0〜350℃が好ましく、300℃以下では熱固定が不
十分で寸法精度が低下する場合が多く、300℃以上に
なると機械的性能が低下する傾向になりがちであり、
又、ヒートセット時間はヒートセット温度によって変化
するが通常10〜30分が好ましく10分未満では熱固
定が充分でなく寸法安定性が低下する場合が多く、30
分以上になるとフィルムの膜厚精度が低下しがちである
が用途によっては、これらの範囲以外の値でも成膜可能
でありかかる値は特に制限されない。
The heat setting, which is performed as necessary, is generally performed continuously as it is after the stretching is completed, but the heat setting is not limited to this and may be performed by any other appropriate method. The heat setting temperature is not particularly limited, but is 30
0 to 350 ° C. is preferable, and if the temperature is 300 ° C. or lower, heat setting is insufficient and the dimensional accuracy is often lowered. If the temperature is 300 ° C. or higher, mechanical performance tends to be lowered.
The heat setting time varies depending on the heat setting temperature, but is usually 10 to 30 minutes, and if it is less than 10 minutes, heat setting is not sufficient and dimensional stability often deteriorates.
If it is more than a minute, the film thickness accuracy of the film tends to decrease, but depending on the application, a film having a value outside these ranges can be formed, and such a value is not particularly limited.

【0020】上記した熱可塑性ポリイミド系フィルムの
成膜はフィルムの中に異物等が混入するのを防止するた
めにクリーンルームで行なう事が望ましいが、このこと
に特に制限されない。この際、クリーンルームのクリー
ン度は1立方フィートの空気中に含まれる0.1μ以上
の粒子の数が10,000以下が好適であり少なければ
少ない程歩留の向上が期待できる。勿論従来の如く敢て
クリーンルームで行なわなくてもよく、用途によっては
通常の室で成膜すればよい。
The above-mentioned thermoplastic polyimide film is preferably formed in a clean room in order to prevent foreign matters from entering the film, but the invention is not particularly limited to this. At this time, the cleanness of the clean room is preferably 10,000 or less in the number of particles of 0.1 μ or more contained in 1 cubic foot of air, and the smaller the number, the higher the yield can be expected. Needless to say, it does not have to be performed in a clean room as in the conventional case, and the film may be formed in an ordinary room depending on the application.

【0021】上記により成膜された熱可塑性ポリイミド
系チューブ状フィルムは耐熱性、機械的特性、寸法安定
性、膜厚精度、難燃性、耐摩擦、摩耗性、電気的特性等
に優れ、フレキシブルプリント基板、電気部品の絶縁用
フィルム、シートベルト、食品用トレー、医療用部品、
光学部品機材等の用途展開が期待でき用途については特
に制限はない。
The thermoplastic polyimide tubular film formed as described above is excellent in heat resistance, mechanical properties, dimensional stability, film thickness accuracy, flame retardancy, abrasion resistance, abrasion resistance, electrical properties, etc. and is flexible. Printed circuit boards, insulating films for electrical parts, seat belts, food trays, medical parts,
There are no particular restrictions on the use of optical parts and equipment as they can be expected to expand.

【0022】以下実施例について本発明を説明する。The present invention will be described below with reference to examples.

【0023】[0023]

【実施例】熱可塑性ポリイミド樹脂のペレット(ガラス
転移温度250℃、融点388℃、高化式フローテスタ
ー420℃で測定した溶融粘度2927ポイズ)を棚段
乾燥機で循環熱風温度300℃で2時間乾燥しペレット
の表面のみを結晶化させた後、密封式の除湿型ホッパー
ドライヤーで250℃、10時間乾燥させ水分含有量1
0ppmにした。次いで、該ペレットをホッパーに供給
し窒素置換しながら、シリンダー温度360〜390℃
に加熱されたシリンダー内面をX−アロイ800(富士
インダストリーズ社製)でライニングされた押出機に送
り込み溶融し、シリンダーの先端とダイスの間に取付け
た度目5μの前記したリーフ型フィルターを通過させ、
外径32φ、内径30φ、温度390℃の環状ダイスか
ら溶融押出した。溶融押出された溶融状フィルムを、真
空水槽方式で内径245φのサイジングスリーブに吸引
させて冷却し熱可塑性ボリイミドチューブ状フィルムを
成膜した。このフィルムは厚み50μ±5μ、周長7
5.4±0.5mmであった。こうして得られたチュー
ブ状フィルムを290℃で円周方向に2倍、縦方向に
1.2倍に延伸した後、310℃で熱セットを行なった
ところ、得られたフィルムは厚み20±2μ、周長15
0.8±0.2mmであった。この熱可塑性ポリイミド
系チューブ状フィルムの成膜はクリーン度10,000
のクリーンルームで成膜したので異物の混入は認められ
なかった。
[Examples] Pellets of a thermoplastic polyimide resin (glass transition temperature 250 ° C, melting point 388 ° C, melt viscosity 2927 poise measured by Koka type flow tester 420 ° C) were circulated in a tray dryer at a hot air temperature of 300 ° C for 2 hours. After drying and crystallizing only the surface of the pellet, it is dried at 250 ° C for 10 hours in a hermetic dehumidifying hopper dryer to obtain a water content of 1
It was set to 0 ppm. Then, while supplying the pellets to the hopper and replacing the atmosphere with nitrogen, the cylinder temperature is 360 to 390 ° C.
The inner surface of the heated cylinder was sent to an extruder lined with X-Alloy 800 (manufactured by Fuji Industries Co., Ltd.) and melted, and passed through the leaf type filter of 5 μm installed between the tip of the cylinder and the die,
Melt extrusion was carried out from an annular die having an outer diameter of 32φ, an inner diameter of 30φ and a temperature of 390 ° C. The melt-extruded molten film was sucked into a sizing sleeve having an inner diameter of 245φ by a vacuum water tank system and cooled to form a thermoplastic polyimide tube film. This film has a thickness of 50μ ± 5μ and a perimeter of 7
It was 5.4 ± 0.5 mm. The thus obtained tubular film was stretched twice at 290 ° C. in the circumferential direction and 1.2 times in the machine direction, and then heat set at 310 ° C. to obtain a film having a thickness of 20 ± 2 μm. Circumference 15
It was 0.8 ± 0.2 mm. The thermoplastic polyimide tube-shaped film has a cleanness of 10,000.
Since the film was formed in the clean room of No. 3, contamination of foreign matter was not recognized.

【0024】[0024]

【比較例】熱硬化型ポリイミド系樹脂では押出成膜出来
なかった。
[Comparative Example] Extrusion film formation could not be performed with a thermosetting polyimide resin.

【0025】[0025]

【発明の効果】本発明は以上の通りである。本発明の熱
可塑性ポリイミド系チューブ状フィルムは特に寸法精
度、膜厚精度に優れる好ましいもので、例えばFPC
(フレキシブルプリント基板)、電線の絶縁用フィル
ム、耐熱性を利用した精密電気電子部材例えば複写機、
プリンターの各種ベルト例えば定着ベルト等に好適であ
り、また寸法精度が良好なので精密機材等の駆動用ベル
トに利用可能である。更に食品用、医療用、光学用部品
の機材、その他あらゆる分野で種々の用途が期待できる
ものである。
The present invention is as described above. The thermoplastic polyimide-based tubular film of the present invention is particularly preferable because it is excellent in dimensional accuracy and film thickness accuracy.
(Flexible printed circuit board), insulation film for electric wire, precision electric / electronic member using heat resistance, such as copying machine,
It is suitable for various belts of printers, such as a fixing belt, and has good dimensional accuracy, so it can be used as a driving belt for precision equipment. Further, it can be expected to be used in various fields such as food, medical, optical parts, and other fields.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 吉田 勉 滋賀県守山市森川原町163番地 グンセ株 式会社滋賀研究所内 (72)発明者 脇中 敏 愛知県江南市大字村久野字平野1番地 グ ンゼ株式会 社江南工場内   ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Tsutomu Yoshida             Gunse Co., 163 Morikawaramachi, Moriyama City, Shiga Prefecture             Shiga Research Institute (72) Inventor Satoshi Wanaka             1 Hirano, Murakuno, Oita, Konan City, Aichi Prefecture             Nze Stock Company Inside the Gangnam Factory

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 熱可塑性ポリイミド系樹脂を主成分とす
る溶融押出成膜されてなる熱可塑性ポリイミド系チュー
ブ状フィルム。
1. A thermoplastic polyimide-based tubular film formed by melt-extrusion film formation containing a thermoplastic polyimide-based resin as a main component.
【請求項2】 耐食性合金マトリックスの中に微粒子物
質が均一に分散されたライニング層で内表面が被覆され
てなるシリンダーを有する押出機により溶融押出成膜さ
れてなる請求項1に記載の熱可塑性ポリイミド系チュー
ブ状フィルム。
2. The thermoplastic resin composition according to claim 1, wherein a melt-extrusion film is formed by an extruder having a cylinder having an inner surface coated with a lining layer in which a fine particle substance is uniformly dispersed in a corrosion-resistant alloy matrix. Polyimide tube film.
【請求項3】 繊維径の大なる金属繊維からなる不織布
と繊維径の小なる金属繊維からなる不織布とを積層した
複合不織布を、保護層と支持層との間に配し焼結してな
る濾過フィルターの取付けられた押出機により溶融押出
成膜されてなる請求項1に記載の熱可塑性ポリイミド系
チューブ状フィルム。
3. A composite non-woven fabric obtained by laminating a non-woven fabric made of metal fibers having a large fiber diameter and a non-woven fabric made of metal fibers having a small fiber diameter, which is placed between a protective layer and a support layer and sintered. The thermoplastic polyimide tubular film according to claim 1, which is formed by melt extrusion film formation by an extruder equipped with a filtration filter.
【請求項4】 押出機に供給する際、水分含有量が30
ppm以下である熱可塑性ポリイミド系樹脂を用いて溶
融押出成膜されてなる請求項1に記載の熱可塑性ポリイ
ミド系チューブ状フィルム。
4. When supplied to an extruder, it has a water content of 30.
The thermoplastic polyimide-based tubular film according to claim 1, wherein the thermoplastic polyimide-based resin having a ppm or less is melt-extruded to form a film.
【請求項5】10,000クラス以下のクリーンルーム
で溶融押出成膜されてなる請求項1に記載の熱可塑性ポ
リイミド系チューブ状フィルム。
5. The thermoplastic polyimide tubular film according to claim 1, which is formed by melt extrusion film formation in a clean room of 10,000 class or less.
JP28094791A 1991-07-31 1991-07-31 Method for producing thermoplastic polyimide resin tubular film Expired - Fee Related JP3237715B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP28094791A JP3237715B2 (en) 1991-07-31 1991-07-31 Method for producing thermoplastic polyimide resin tubular film
US08/232,312 US5389412A (en) 1991-07-31 1994-04-25 Thermoplastic polyimide tubular film

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP28094791A JP3237715B2 (en) 1991-07-31 1991-07-31 Method for producing thermoplastic polyimide resin tubular film
US08/232,312 US5389412A (en) 1991-07-31 1994-04-25 Thermoplastic polyimide tubular film

Publications (2)

Publication Number Publication Date
JPH0531781A true JPH0531781A (en) 1993-02-09
JP3237715B2 JP3237715B2 (en) 2001-12-10

Family

ID=26553992

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28094791A Expired - Fee Related JP3237715B2 (en) 1991-07-31 1991-07-31 Method for producing thermoplastic polyimide resin tubular film

Country Status (1)

Country Link
JP (1) JP3237715B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7445853B2 (en) * 2002-10-17 2008-11-04 Nv Bekaert Sa Layered filter structure comprising short metal fibers

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7445853B2 (en) * 2002-10-17 2008-11-04 Nv Bekaert Sa Layered filter structure comprising short metal fibers

Also Published As

Publication number Publication date
JP3237715B2 (en) 2001-12-10

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