JPH022409B2 - - Google Patents

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Publication number
JPH022409B2
JPH022409B2 JP57087246A JP8724682A JPH022409B2 JP H022409 B2 JPH022409 B2 JP H022409B2 JP 57087246 A JP57087246 A JP 57087246A JP 8724682 A JP8724682 A JP 8724682A JP H022409 B2 JPH022409 B2 JP H022409B2
Authority
JP
Japan
Prior art keywords
film
heat
temperature
density
phenylene sulfide
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
JP57087246A
Other languages
Japanese (ja)
Other versions
JPS58205733A (en
Inventor
Takashi Kawamura
Toshinori Sugie
Fumihiro Furuhata
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.)
DIC Corp
Original Assignee
Dainippon Ink and Chemicals 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 Dainippon Ink and Chemicals Co Ltd filed Critical Dainippon Ink and Chemicals Co Ltd
Priority to JP57087246A priority Critical patent/JPS58205733A/en
Publication of JPS58205733A publication Critical patent/JPS58205733A/en
Priority to US06/816,312 priority patent/US4629778A/en
Publication of JPH022409B2 publication Critical patent/JPH022409B2/ja
Granted legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G75/00Macromolecular compounds obtained by reactions forming a linkage containing sulfur with or without nitrogen, oxygen, or carbon in the main chain of the macromolecule
    • C08G75/02Polythioethers
    • C08G75/0204Polyarylenethioethers
    • C08G75/0277Post-polymerisation treatment
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2381/00Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing sulfur with or without nitrogen, oxygen, or carbon only; Polysulfones; Derivatives of such polymers
    • C08J2381/02Polythioethers; Polythioether-ethers

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は寸法安定性に優れたポリp―フエニレ
ンスルフイドフイルムの製造方法に関するもので
ある。 従来、ポリエチレンテレフタレート(以下
PETと略す)フイルムは、その機械的特性、寸
法安定性、電気特性、透明性、耐薬品性などの良
さを活かして絶縁用フイルム、磁気テープのベー
スフイルム、写真用ベースフイルム、包装用フイ
ルムなど種々の分野で使用されている。しかし、
PETフイルムの欠点は耐熱性にあり、その連続
使用温度は耐熱タイプのものでも130℃しかない。
現在耐熱性フイルムとしてはポリイミドフイルム
があり、その非常にすぐれた耐熱性を利用して、
宇宙、航空機用素材や高級電気絶縁用素材として
使用されている。そして省エネルギーの重要性や
種々の産業機器の小型化、軽量化、高性能化、信
頼性の向上などの要求により、その用途および使
用量は年々拡大されつつある。しかし、このポリ
イミドフイルムは溶液製膜法により作られるため
生産性が悪く、コストも高いという欠点をもつて
いる。そこで、PETフイルムより耐熱性にすぐ
れ、かつ溶融成形可能な生産性の良いフイルムと
して特開昭54−142275号にみられるようにポリp
―フエニレンスルフイドフイルムが知られてい
る。 ポリp―フエニレンスルフイドフイルムを2軸
延伸したものは特開昭56−62128号などにみられ
るようにほとんど非晶質のポリp―フエニレンス
ルフイドの未延伸シートまたはフイルムを80〜
120℃の温度範囲で一方向あるいは二方向に延伸
し、その延伸フイルムのTm(融点)を越えない
温度範囲で熱固定することによつて得られてい
る。このような製造工程の中で熱固定温度はTm
未満の温度で行われる。すなわち、熱固定温度は
150〜280℃である。しかし、このような温度範囲
でポリp―フエニレンスルフイドフイルムを熱固
定した場合、特開昭56−62121号でみられるよう
に200℃での熱収縮率が約1.0%程度であり、加熱
下における寸法安定性がよくないという欠点があ
つた。 本発明者らはこの点に注目し、新しい熱固定方
法について鋭意研究した結果、特定の温度範囲で
熱固定することにより加熱下における寸法安定性
の良好なフイルムを短時間で得られることを見出
し、本発明に到達したものである。 すなわち、本発明は縦横二方向に延伸し配向さ
せた2軸延伸ポリp―フエニレンスルフイドフイ
ルムをTm〜350℃の温度範囲で熱固定すること
を特徴とするポリp―フエニレンスルフイドフイ
ルムの製造方法に関するものである。 本発明のポリp―フエニレンスルフイドはその
90モル%以上が構成単位
The present invention relates to a method for producing poly p-phenylene sulfide film having excellent dimensional stability. Conventionally, polyethylene terephthalate (hereinafter referred to as
PET (abbreviated as PET) film takes advantage of its mechanical properties, dimensional stability, electrical properties, transparency, and chemical resistance to be used as insulation film, base film for magnetic tape, photographic base film, packaging film, etc. Used in various fields. but,
The disadvantage of PET film is its heat resistance, and even the heat-resistant type can only be used continuously at a temperature of 130°C.
Polyimide film is currently available as a heat-resistant film, and taking advantage of its excellent heat resistance,
It is used as a space and aircraft material and as a high-grade electrical insulation material. Due to the importance of energy conservation and demands for smaller, lighter weight, higher performance, and improved reliability of various industrial equipment, their applications and usage are expanding year by year. However, since this polyimide film is produced by a solution casting method, it has the drawbacks of poor productivity and high cost. Therefore, as a film that has better heat resistance than PET film and can be melt-molded and has good productivity, polyp
- Phenylene sulfide film is known. Biaxially stretched poly p-phenylene sulfide film is disclosed in JP-A No. 56-62128, etc., where an unstretched sheet or film of almost amorphous poly p-phenylene sulfide is ~
It is obtained by stretching in one or two directions at a temperature of 120°C and heat-setting at a temperature that does not exceed the Tm (melting point) of the stretched film. In this manufacturing process, the heat setting temperature is Tm
carried out at temperatures below. In other words, the heat fixation temperature is
The temperature is 150-280℃. However, when poly p-phenylene sulfide film is heat-set in such a temperature range, the heat shrinkage rate at 200°C is about 1.0%, as seen in JP-A-56-62121. The drawback was poor dimensional stability under heating. The inventors of the present invention focused on this point, and as a result of intensive research into a new heat-setting method, they discovered that by heat-setting within a specific temperature range, a film with good dimensional stability under heating can be obtained in a short time. , the present invention has been achieved. That is, the present invention provides a poly p-phenylene sulfide film, which is characterized by heat-setting a biaxially stretched poly p-phenylene sulfide film stretched and oriented in both the longitudinal and lateral directions at a temperature range of Tm to 350°C. The present invention relates to a method for producing an id film. The poly p-phenylene sulfide of the present invention is
More than 90 mol% is a constituent unit

【式】から 成るポリマーであることが好ましく、90モル%よ
り少ないと結晶性が低下する上に耐熱性、機械的
特性などの低下をきたすのみなず、寸法安定性に
も悪影響を与える。かかるポリp―フエニレンス
ルフイドは10モル%未満であれば例えばメタ結合
A polymer consisting of the formula is preferred; if the amount is less than 90 mol%, not only will crystallinity decrease, heat resistance and mechanical properties deteriorate, but also dimensional stability will be adversely affected. If the poly p-phenylene sulfide is less than 10 mol %, it may form a meta bond, for example.

【式】エーテル結合[Formula] Ether bond

【式】ビフエニル結 合[Formula] Biphenyl linkage If

【式】ナフタレン結合[Formula] Naphthalene bond

【式】スルホン結合[Formula] Sulfone bond

【式】置換フエニ レンスルフイド結合[Formula] Substituted Feni Rensulfide bond

【式】ここでR はアルキル、ニトロ、フエニル、アルコキシ、ス
ルホン、ハロゲン、カルボン酸、カルボン酸の金
属塩などである)、および前述の3官能フエニレ
ンスルフイド結合
[Formula] where R is alkyl, nitro, phenyl, alkoxy, sulfone, halogen, carboxylic acid, metal salt of carboxylic acid, etc.), and the aforementioned trifunctional phenylene sulfide bond.

【式】などを含有 していてもよい。 このようなポリp―フエニレンスルフイドを押
出機、プレス等によりシート又はフイルム状に成
形した後、液体チツ素、水、ロール等を使用して
急冷することにより密度が1.330g/cm3以下とな
り、ほとんど非晶質の未延伸フイルムが得られ
る。未延伸フイルムの結晶化が進行していると結
晶粒子が延伸性を低下させ、延伸時にフイルムの
破断が生じやすくなる。 未延伸フイルムの延伸温度はポリマーの分子量
や成分によつて多少の相違はあるが、通常ポリマ
ーのガラス転移温度付近が望ましい。具体的には
80〜120℃、好ましくは90〜110℃である。延伸方
法としては通常用いられているロール法、テンタ
ー法、チユーブラー法などによる延伸方法が便利
である。延伸倍率は得られるフイルムの物性、生
産性からみて2.5〜7.0倍、好ましくは3.0〜5.5倍
とするのが良く、同時2軸延伸、逐次2軸延伸の
どちらを用いてもよい。 このようにして得られた2軸延伸フイルムは透
明性を失わないように結晶化度を上げるために
Tm〜350℃、好ましくはTm〜330℃の温度範囲
で通常、120秒以内の時間で熱処理される。ここ
でTmは2軸延伸直後の熱処理前のフイルムの示
差走査熱量計(以下DSCと称す)で測定される
融点である。この際、350℃を越える熱処理温度
では熱処理時間を短くしてもフイルムが溶融状態
になり、フイルムの形状を保つことができなくな
つてしまう。Tm〜350℃の熱処理温度であれば
120秒以内で熱処理時間を適度に調整することに
よりフイルムが溶融状態にならず熱固定ができ、
かつTm未満の温度で熱固定した場合よりも密度
が上昇し、加熱下における寸法安定性が向上す
る。またこの熱固定の際、縦横方向に適度な制限
収縮を与えた状態で、あるいは定長下また緊張下
で熱固定を行うことはさしつかえない。一般に、
PETフイルムで代表される結晶性ポリマーフイ
ルムの熱固定温度はそのポリマーの融点以下で行
われている。本発明のようにポリマーの融点以上
の温度で熱固定することは全く新しい熱固定方法
である。 本発明における熱固定は加熱された気体又は液
体の流れあるいは固体の表面に熱固定前の延伸フ
イルムを接触させることによつて行われる。ま
た、赤外線ヒータなどのような輻射熱を利用する
こともできる。更に、超音波、高周波を照射して
も良い。本発明における熱固定の「温度」および
「時間」とは媒体使用の場合には加熱媒体の温度
および加熱媒体への延伸フイルムの接触時間のこ
とである。また、赤外線ヒーター、超音波、高周
波等の使用の場合にはフイルム温度および処理時
間をいう。 このようにして得られる本発明のフイルムは結
晶化度が高く、加熱下における寸法安定性がすぐ
れ、また融点付近まで加熱しても白化やぜい化を
起さない。 本発明のフイルムは、耐熱性、寸法安定性、機
械的特性にすぐれるため電気絶縁用フイルム、磁
気記録用フイルムとして最適である。例えばフレ
キシブルプリント配線板用ベースフイルム、車両
用モーター、冷凍機用モーターなどの各種回転機
および各種静止器などの絶縁材料として、また一
般ケーブル、高圧、超高圧ケーブルの被覆用絶縁
材料、磁気テープ用ベースフイルム、コンデンサ
ー用フイルムとして有用である。その他、包装
用、農業用、写真用、粘着テープ用ベース、建材
用、装飾用などのフイルム素材として使用するこ
とができる。また他のフイルムとのラミネート、
金属や紙などとの組合せによる複合材としての使
用も可能である。 本発明に於けるガラス転移温度、Tm、密度、
結晶化度の測定方法について述べる。 ガラス転移温度は延伸前の未延伸非晶フイルム
又はシートをTmは2軸延伸直後のフイルムをそ
れぞれ測定用試料としてDSCを用いて常法によ
り測定される。 密度は臭化リチウム水溶液を用いて密度勾配管
により求められる。結晶化度(Xc)は上述した
密度を用いて密度法により求められる。すなわち
Xcは一般に用いられる次の式より求められる。 1/d=Xc/dcr+1−Xc/dam ……(1) 式(1)においてd,dcrおよびdamはそれぞれ試
料の密度、結晶相の密度および非結晶相の密度で
ある。ここでdcr,damはEur,poly.J.,7,
1127(1971)で求められている値を用いた。すな
わち、dcr=1.430g/cm3、dam=1.320g/cm3
ある。 実施例1〜3、比較例1〜3 5スケールのオートクレーブにN―メチルピ
ロリドン1.8Kg、硫化ナトリウム(59.6%純度)
0.5Kg、安息香酸ナトリウム0.6Kg、水酸化ナトリ
ウム1.6gを仕込み、チツ素気流中で200℃まで昇
温し、脱水率53%まで脱水を行つた。系を160℃
まで冷却後、p―ジクロルベンゼン0.6Kg仕込み
封をして、チツ素で内圧を4Kg/cm3まで加圧し
た。重合による発熱の昇温速度を制御しながらコ
ントロールし、250℃まで昇温して3時間撹拌し
ながら重合を行つた。次に系を冷却後放圧し、内
容物を水中にあけ、粉末のポリマーを取り出し、
水、アセトンで洗浄をくり返した。このポリマー
を120℃で3時間乾燥し、白色粉末のポリマーを
得た。このポリマーの溶液粘度〔η〕をα―クロ
ルナフタリンを用いて温度206℃、濃度0.4Kg/
100mlで測定したところ0.30dl/gであつた。こ
のポリマー320℃にてプレスにより製膜後、水中
で急冷して密度1.321g/cm3、厚さ405ミクロンを
有する透明なほとんど非晶質の未延伸シートを得
た。この非晶シートのガラス転移温度をDSCで
昇温速度20℃/分で測定したところ89℃であつ
た。 この非晶シートを94℃で3.5×3.5倍の同時2軸
延伸を行つた。この延伸フイルムのTmはDSCで
昇温速度20℃/分で測定したところ284℃であつ
た。このフイルム表―1に示すような温度および
時間で定長下で熱固定を行つた。比較例として
Tm未満で実施例と同様に熱固定を行つた。これ
らのフイルムの密度、結晶化度および熱収縮率を
測定し、結果を表―1に示した。本発明における
フイルムは密度および結晶化度が高く、かつ熱収
縮率が小さく加熱下における寸法安定性がすぐれ
ているという特徴を有している。 実施例4〜6、比較例4〜7 実施例1〜3で用いた非晶シートを95℃にて縦
3.5×横4.0倍の遂次2軸延伸を行い、実施例1〜
3と同様にTmを測定したところ286℃であつた。
このフイルムを表―2に示すような温度および時
間で定長下で熱固定を行つた。比較例としてTm
未満で実施例と同様に熱固定を行つた。これらの
フイルムの密度、結晶化度、熱収縮率を測定し、
結果を表―2に示した。本発明によるフイルムは
加熱下における寸法安定性の良好なフイルムであ
る。
[Formula] etc. may be included. Such poly p-phenylene sulfide is formed into a sheet or film using an extruder, press, etc., and then rapidly cooled using liquid nitrogen, water, a roll, etc. to a density of 1.330 g/cm 3 As a result, an almost amorphous unstretched film is obtained. When the crystallization of the unstretched film progresses, the crystal particles reduce the stretchability and the film becomes more likely to break during stretching. Although the stretching temperature of the unstretched film varies somewhat depending on the molecular weight and components of the polymer, it is usually desirable to draw the unstretched film around the glass transition temperature of the polymer. in particular
The temperature is 80-120°C, preferably 90-110°C. As the stretching method, commonly used stretching methods such as a roll method, a tenter method, and a tubular method are convenient. The stretching ratio is preferably 2.5 to 7.0 times, preferably 3.0 to 5.5 times, in view of the physical properties and productivity of the resulting film, and either simultaneous biaxial stretching or sequential biaxial stretching may be used. In order to increase the crystallinity of the biaxially stretched film obtained in this way without losing its transparency,
Heat treatment is carried out at a temperature range of Tm to 350°C, preferably Tm to 330°C, usually for a time of 120 seconds or less. Here, Tm is the melting point of the film immediately after biaxial stretching and before heat treatment, as measured by a differential scanning calorimeter (hereinafter referred to as DSC). At this time, if the heat treatment temperature exceeds 350°C, the film will become molten even if the heat treatment time is shortened, and the film will not be able to maintain its shape. If the heat treatment temperature is Tm~350℃
By appropriately adjusting the heat treatment time within 120 seconds, the film can be heat-set without becoming molten.
Moreover, the density increases and the dimensional stability under heating is improved compared to when heat setting is performed at a temperature below Tm. In addition, during this heat setting, it is permissible to heat set with appropriate limited shrinkage in the longitudinal and lateral directions, or under constant length or tension. in general,
The heat setting temperature of crystalline polymer films, typified by PET films, is below the melting point of the polymer. Heat setting at a temperature higher than the melting point of the polymer as in the present invention is a completely new heat setting method. Heat setting in the present invention is carried out by bringing the stretched film before heat setting into contact with a stream of heated gas or liquid or the surface of a solid. It is also possible to use radiant heat such as an infrared heater. Furthermore, ultrasonic waves or high frequency waves may be irradiated. In the present invention, the "temperature" and "time" of heat setting refer to the temperature of the heating medium and the contact time of the stretched film to the heating medium when a medium is used. Also, in the case of using an infrared heater, ultrasonic wave, high frequency, etc., it refers to the film temperature and processing time. The film of the present invention thus obtained has a high degree of crystallinity, excellent dimensional stability under heating, and does not cause whitening or embrittlement even when heated to near the melting point. The film of the present invention has excellent heat resistance, dimensional stability, and mechanical properties, and is therefore most suitable as an electrically insulating film or a magnetic recording film. For example, as a base film for flexible printed wiring boards, as an insulating material for various rotating machines and stationary devices such as vehicle motors and refrigerator motors, as an insulating material for covering general cables, high voltage and ultra-high voltage cables, and for magnetic tape. Useful as base film and capacitor film. In addition, it can be used as a film material for packaging, agriculture, photography, adhesive tape bases, building materials, decorations, etc. Also lamination with other films,
It is also possible to use it as a composite material by combining it with metal, paper, etc. Glass transition temperature, Tm, density in the present invention,
The method for measuring crystallinity will be described. The glass transition temperature is measured by a conventional method using DSC using an unstretched amorphous film or sheet before stretching, and Tm using a film immediately after biaxial stretching as measurement samples. Density is determined using a density gradient tube using an aqueous lithium bromide solution. Crystallinity (Xc) is determined by the density method using the density described above. i.e.
Xc is obtained from the following commonly used formula. 1/d=Xc/dcr+1-Xc/dam (1) In equation (1), d, dcr, and dam are the density of the sample, the density of the crystalline phase, and the density of the amorphous phase, respectively. Here dcr, dam is Eur, poly.J., 7,
1127 (1971) was used. That is, dcr=1.430g/cm 3 and dam=1.320g/cm 3 . Examples 1-3, Comparative Examples 1-3 1.8Kg of N-methylpyrrolidone and sodium sulfide (59.6% purity) in a 5 scale autoclave
0.5 kg of sodium benzoate, 0.6 kg of sodium benzoate, and 1.6 g of sodium hydroxide were charged, and the temperature was raised to 200° C. in a nitrogen gas flow, and dehydration was performed to a dehydration rate of 53%. System at 160℃
After cooling, 0.6 kg of p-dichlorobenzene was charged and sealed, and the internal pressure was increased to 4 kg/cm 3 with nitrogen. The rate of temperature increase due to the heat generated by polymerization was controlled, the temperature was raised to 250°C, and polymerization was carried out while stirring for 3 hours. Next, after cooling the system, the pressure was released, the contents were poured into water, and the powdered polymer was taken out.
Washing was repeated with water and acetone. This polymer was dried at 120°C for 3 hours to obtain a white powder polymer. The solution viscosity [η] of this polymer was determined using α-chlornaphthalene at a temperature of 206℃ and a concentration of 0.4Kg/
When measured in 100 ml, it was 0.30 dl/g. This polymer was formed into a film by pressing at 320° C. and then rapidly cooled in water to obtain a transparent, almost amorphous, unstretched sheet having a density of 1.321 g/cm 3 and a thickness of 405 microns. The glass transition temperature of this amorphous sheet was measured by DSC at a heating rate of 20°C/min and found to be 89°C. This amorphous sheet was subjected to simultaneous biaxial stretching of 3.5×3.5 times at 94°C. The Tm of this stretched film was 284°C as measured by DSC at a heating rate of 20°C/min. This film was heat-set at a fixed length at the temperature and time shown in Table 1. As a comparative example
Heat setting was carried out in the same manner as in the examples below Tm. The density, crystallinity and heat shrinkage of these films were measured and the results are shown in Table 1. The film of the present invention is characterized by high density and crystallinity, low thermal shrinkage rate, and excellent dimensional stability under heating. Examples 4 to 6, Comparative Examples 4 to 7 The amorphous sheets used in Examples 1 to 3 were vertically heated at 95°C.
Successive biaxial stretching of 3.5×4.0 times in width was performed, and Example 1~
When Tm was measured in the same manner as in 3, it was 286°C.
This film was heat-set under constant length at the temperature and time shown in Table 2. As a comparative example, Tm
Heat setting was carried out in the same manner as in the examples. The density, crystallinity, and heat shrinkage rate of these films were measured,
The results are shown in Table-2. The film according to the present invention has good dimensional stability under heating.

【表】【table】

【表】 表―1および表―2における熱収縮率は幅10
mm、長さ150mmのフイルムに長さ方向に100mm間隔
の標線を設けたフイルムを表に示された各温度の
乾燥機中に弛緩状態で30分間放置後、フイルムを
乾燥機から取り出し、標線間隔を測定し、その時
の収縮率として求めた。
[Table] The heat shrinkage rate in Table-1 and Table-2 is width 10
A film with a length of 150 mm and marked lines at 100 mm intervals in the length direction was left in a dryer at each temperature shown in the table in a relaxed state for 30 minutes, then the film was removed from the dryer and marked with marks. The line spacing was measured and the shrinkage rate at that time was determined.

Claims (1)

【特許請求の範囲】[Claims] 1 縦横二方向に延伸し配向させた2軸配向ポリ
フエニレンスルフイドフイルムをTm(Tm:2軸
延伸直後のフイルムの融点)〜350℃の温度範囲
で熱固定することを特徴とするポリp―フエニレ
ンスルフイドフイルムの製造方法。
1. A polyp characterized by heat-setting a biaxially oriented polyphenylene sulfide film stretched and oriented in both the vertical and horizontal directions at a temperature range of Tm (Tm: melting point of the film immediately after biaxial stretching) to 350°C. -Production method of phenylene sulfide film.
JP57087246A 1982-05-20 1982-05-25 Production of poly-p-phenylene sulfide film Granted JPS58205733A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP57087246A JPS58205733A (en) 1982-05-25 1982-05-25 Production of poly-p-phenylene sulfide film
US06/816,312 US4629778A (en) 1982-05-20 1986-01-06 Poly(p-phenylene sulfide) film and process for production thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57087246A JPS58205733A (en) 1982-05-25 1982-05-25 Production of poly-p-phenylene sulfide film

Publications (2)

Publication Number Publication Date
JPS58205733A JPS58205733A (en) 1983-11-30
JPH022409B2 true JPH022409B2 (en) 1990-01-18

Family

ID=13909442

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57087246A Granted JPS58205733A (en) 1982-05-20 1982-05-25 Production of poly-p-phenylene sulfide film

Country Status (1)

Country Link
JP (1) JPS58205733A (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5662126A (en) * 1979-10-26 1981-05-27 Toray Ind Inc Manufacture of polyphenylene sulfide film

Also Published As

Publication number Publication date
JPS58205733A (en) 1983-11-30

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