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TWI698462B - Polyimide film - Google Patents

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TWI698462B
TWI698462B TW105107078A TW105107078A TWI698462B TW I698462 B TWI698462 B TW I698462B TW 105107078 A TW105107078 A TW 105107078A TW 105107078 A TW105107078 A TW 105107078A TW I698462 B TWI698462 B TW I698462B
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film
polyimide film
polyimide
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gel
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TW201714921A (en
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我妻亮作
大場大史
平松直比古
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日商東麗 杜邦股份有限公司
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    • C08G73/00Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
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    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00Shaping by stretching, e.g. drawing through a die; Apparatus therefor
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    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B29C55/00Shaping by stretching, e.g. drawing through a die; Apparatus therefor
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    • B29C55/12Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B15/00Layered products comprising a layer of metal
    • B32B15/04Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material
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    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G73/00Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
    • C08G73/06Polycondensates having nitrogen-containing heterocyclic rings in the main chain of the macromolecule
    • C08G73/10Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
    • C08G73/1042Copolyimides derived from at least two different tetracarboxylic compounds or two different diamino compounds
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    • C08G73/00Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
    • C08G73/06Polycondensates having nitrogen-containing heterocyclic rings in the main chain of the macromolecule
    • C08G73/10Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
    • C08G73/1046Polyimides containing oxygen in the form of ether bonds in the main chain
    • C08G73/105Polyimides containing oxygen in the form of ether bonds in the main chain with oxygen only in the diamino moiety
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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    • C08G73/00Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
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    • C08G73/10Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
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    • C08G73/1071Wholly aromatic polyimides containing oxygen in the form of ether bonds in the main chain
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2379/00Other polymers having nitrogen, with or without oxygen or carbon only, in the main chain
    • B32B2379/08Polyimides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2457/00Electrical equipment
    • B32B2457/08PCBs, i.e. printed circuit boards
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    • C08J2379/00Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen, or carbon only, not provided for in groups C08J2361/00 - C08J2377/00
    • C08J2379/04Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
    • C08J2379/08Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors

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Abstract

本發明之課題在於提供一種即便浸漬於鹼性溶液中亦不易發生由膜之變質及/或水解所導致之特性劣化、且厚度為1.0~10.0μm之薄聚醯亞胺膜。 The subject of the present invention is to provide a thin polyimide film with a thickness of 1.0 to 10.0 μm, which is not prone to deterioration in characteristics caused by film deterioration and/or hydrolysis even if it is immersed in an alkaline solution.

將厚度為1.0~10.0μm之聚醯亞胺膜之L值設為28~45,又,於將聚醯亞胺之重複單元之分子量設為100%時,將其醯亞胺基之分子量設為40%以下。 Set the L value of the polyimide film with a thickness of 1.0~10.0μm to 28~45, and when the molecular weight of the polyimide repeating unit is set to 100%, set the molecular weight of the polyimide group to Less than 40%.

Description

聚醯亞胺膜 Polyimide film

本發明係關於一種耐鹼化學品性優異之極薄聚醯亞胺膜。 The present invention relates to an extremely thin polyimide film with excellent alkali chemical resistance.

使芳香族二胺、與芳香族四羧酸二酐於有機溶劑中進行聚合反應而獲得聚醯胺酸聚合物溶液後,將該聚醯胺酸聚合液形成為膜狀,使其進行熱脫水閉環及/或化學脫水閉環、即醯亞胺化,藉此而獲得之聚醯亞胺膜因耐熱性、絕緣性及機械特性優異,故被廣泛用於電線之電絕緣材料、隔熱材料、柔性印刷基板(以下簡稱為FPC)之基礎膜、IC(Integrated Circuit,積體電路)之捲帶自動接合用之載帶膜、IC之引線框架固定用膠帶、以導電性電路之保護或絕緣為目的之覆蓋層用途等中。 After the aromatic diamine and the aromatic tetracarboxylic dianhydride are polymerized in an organic solvent to obtain a polyamide acid polymer solution, the polyamide acid polymer solution is formed into a film shape and subjected to thermal dehydration The polyimide film obtained by closed loop and/or chemical dehydration closed loop, that is, imidization, is widely used in electrical insulation materials, thermal insulation materials, and electrical insulation materials for electric wires because of its excellent heat resistance, insulation and mechanical properties. Flexible printed circuit board (hereinafter referred to as FPC) base film, IC (Integrated Circuit, integrated circuit) tape carrier film for automatic bonding, IC lead frame fixing tape, conductive circuit protection or insulation In the purpose of covering layer use, etc.

該等用途中,FPC係將於柔軟且較薄之基礎膜上形成電路圖案並於其表面上施加覆蓋層而成者作為基本結構,由於其可撓性等優秀特性,而被廣泛用於電子技術領域中。近年來,由於封裝技術之進步而推進佈線之高密度化、FPC之多層化,伴隨於此而亦要求高耐彎曲性。作為FPC之耐彎曲性提高及小型化之手段之一,有效的是薄膜化,自先前之銅箔/接著劑(丙烯酸系或者環氧系樹脂)/聚醯亞胺之3層類型以來,不插入接著劑之銅箔/聚醯亞胺之2層類型成為主流。 Among these applications, FPC will form a circuit pattern on a soft and thin base film and apply a covering layer on its surface as the basic structure. Due to its excellent properties such as flexibility, it is widely used in electronics. In the technical field. In recent years, due to advances in packaging technology, high-density wiring and multi-layer FPC have been promoted, and high bending resistance has also been required along with this. As one of the means of improving the bending resistance and miniaturization of FPC, thin film is effective. Since the previous three-layer type of copper foil/adhesive (acrylic or epoxy resin)/polyimide, no The two-layer type of copper foil/polyimide inserted with adhesive has become the mainstream.

作為銅箔/聚醯亞胺之2層類型之製作方法,除了於銅箔上澆鑄聚醯亞胺前驅物樹脂而製作之澆鑄法以外,可列舉如下方法:於加熱前之非熱塑性聚醯亞胺膜之單面或者兩面上塗佈作為熱塑性聚醯亞胺之 前驅物之聚醯胺酸之有機溶劑溶液,然後進行加熱而獲得膜後,貼合銅箔之方法;於加熱後之非熱塑性聚醯亞胺膜之單面或者兩面上塗佈作為熱塑性聚醯亞胺之前驅物之聚醯胺酸之有機溶劑溶液,貼合銅箔之方法等。 As a production method of the two-layer type of copper foil/polyimide, in addition to the casting method of casting polyimide precursor resin on the copper foil, the following methods can be cited: non-thermoplastic polyimide before heating One or both sides of the amine film are coated as a thermoplastic polyimide The organic solvent solution of polyamide acid as the precursor is heated to obtain the film, and then the copper foil is laminated; the heated non-thermoplastic polyimide film is coated on one or both sides as a thermoplastic polyamide The organic solvent solution of polyamide acid as the precursor of imine, the method of laminating copper foil, etc.

作為該等FPC用途之聚醯亞胺膜,近年來謀求薄膜化,但存在如下問題:因薄膜化導致膜之強度減弱,於膜或FPC之製造步驟中,容易發生膜之斷裂或變形。又,厚度越薄則膜之剛性越降低,故存在膜之平面性變差,於搬送膜時容易產生皺褶,成品率降低之問題。 As these polyimide films for FPC applications, thinning has been sought in recent years, but there is a problem that the strength of the film is weakened due to the thinning, and the film is likely to be broken or deformed during the manufacturing steps of the film or FPC. In addition, the thinner the thickness, the lower the rigidity of the film, so the flatness of the film deteriorates, wrinkles are likely to occur when the film is transported, and the yield is reduced.

尤其若欲製作厚度為10.0μm以下之極薄聚醯亞胺膜,則存在以下問題:由於其較薄,故非常容易產生膜端部之自經針固定之孔的破裂、或由搬送時之皺褶之產生所致的膜蜿蜒而破損等故障,生產性較低。 In particular, if an ultra-thin polyimide film with a thickness of 10.0 μm or less is to be produced, the following problems exist: because of its thinness, it is very easy to cause rupture at the end of the film from the needle-fixed hole, or when it is transported. Troubles such as winding and breakage of the film caused by the occurrence of wrinkles are low in productivity.

作為不易產生製膜中之膜破損或搬送時之皺褶等問題、厚度為8.0μm以下之極薄聚醯亞胺膜,報告有規定了膜之抗撕裂擴大阻力或超音波傳輸速度之膜(專利文獻1)。 As an ultra-thin polyimide film with a thickness of less than 8.0μm, which is unlikely to cause film breakage or wrinkles during film production, it has been reported that the film has a specified tear resistance expansion resistance or ultrasonic transmission speed. (Patent Document 1).

又,作為極薄聚醯亞胺膜之製造方法,報告有將含有脫模劑之聚醯亞胺樹脂前驅物溶液塗佈於基材上,進行乾燥及熱處理後自基材剝離之方法等(專利文獻2)。 In addition, as a method for producing ultra-thin polyimide film, a method of coating a polyimide resin precursor solution containing a release agent on a substrate, drying and heat treatment, and peeling from the substrate, etc. ( Patent Document 2).

[先前技術文獻] [Prior Technical Literature] [專利文獻] [Patent Literature]

[專利文獻1]日本專利特開2014-196467號公報 [Patent Document 1] Japanese Patent Laid-Open No. 2014-196467

[專利文獻2]日本專利特開2009-226632號公報 [Patent Document 2] Japanese Patent Laid-Open No. 2009-226632

然而,若使聚醯亞胺膜薄至10.0μm以下,則對化學品之耐久性容易降低成問題。例如於FPC製造步驟中之乾抗蝕膜之剝離步驟中,於作為剝離液之鹼性溶液中浸漬了幾分鐘之時,越為薄之聚醯亞胺膜,變質速度越快而越變硬變脆,由此產生其斷裂強度或斷裂伸長率 之降低、裂縫等,大大損及FPC之可靠性。故而,要求開發出耐鹼性優異之極薄聚醯亞胺膜。 However, if the polyimide film is made as thin as 10.0 μm or less, the durability against chemicals tends to be reduced and it becomes a problem. For example, in the peeling step of the dry resist film in the FPC manufacturing process, when immersed in an alkaline solution as a peeling liquid for several minutes, the thinner the polyimide film, the faster the deterioration rate and the harder it becomes. Become brittle, resulting in its breaking strength or elongation at break The reduction, cracks, etc. greatly damage the reliability of the FPC. Therefore, it is required to develop an extremely thin polyimide film with excellent alkali resistance.

本發明之目的在於提供一種即便浸漬於鹼性溶液中亦不易於發生由膜之變質及/或水解所導致之特性劣化、且厚度為1.0~10.0μm之薄聚醯亞胺膜。 The object of the present invention is to provide a thin polyimide film with a thickness of 1.0 to 10.0 μm, which is not prone to deterioration in characteristics caused by film deterioration and/or hydrolysis even if it is immersed in an alkaline solution.

又,本發明之課題亦在於提供一種於膜製造步驟中不產生破損或皺褶、製膜穩定性優異之厚度為1.0~10.0μm的薄聚醯亞胺膜。 In addition, the subject of the present invention is also to provide a thin polyimide film with a thickness of 1.0 to 10.0 μm that does not cause breakage or wrinkles in the film manufacturing step, and is excellent in film formation stability.

作為提高聚醯亞胺膜之耐鹼性之方法,例如可想到對形成聚醯胺酸之單體之種類或組成進行研究等各種各樣之方法。 As a method of improving the alkali resistance of the polyimide film, for example, various methods such as studies on the type or composition of the monomer forming the polyimide acid are conceivable.

然而,具有較高耐鹼性之先前之薄膜聚醯亞胺膜由於堅硬、柔軟性較差、變脆,故於膜之製造步驟中,產生於膜搬送時膜破損、或由破損之膜屑等導致膜表面產生缺陷之問題,製造膜時之製膜穩定性較差,製膜困難。 However, the previous thin-film polyimide film with higher alkali resistance is hard, less flexible, and brittle. Therefore, during the film manufacturing process, the film is damaged during film transportation, or from damaged film debris. This leads to the problem of defects on the surface of the film, poor film formation stability when manufacturing the film, and difficulty in film formation.

本發明者等人為了解決上述問題而反覆銳意研究,結果發現:藉由將聚醯亞胺膜之L值(進一步而言為聚醯亞胺中之醯亞胺基之比例)調整至特定範圍內,即便為1.0~10.0μm之薄膜,亦可獲得具有耐鹼性(進一步而言為製造膜時之製膜穩定性)之聚醯亞胺膜。 In order to solve the above-mentioned problems, the inventors have made repeated research and found that by adjusting the L value of the polyimide film (furthermore, the ratio of the polyimide group) to a specific range Inside, even if it is a film of 1.0~10.0μm, a polyimide film with alkali resistance (more specifically, film formation stability during film production) can be obtained.

本發明者等人為了解決上述問題而進一步反覆銳意研究,結果完成了本發明。 In order to solve the above-mentioned problems, the inventors of the present invention made further and intensive studies, and as a result, completed the present invention.

即,本發明係關於以下聚醯亞胺膜等。 That is, the present invention relates to the following polyimide film and the like.

〔1〕一種厚度為1.0~10.0μm之聚醯亞胺膜,其特徵在於:將聚醯亞胺之重複單元之分子量設為100%時,其醯亞胺基之分子量為40%以下,且聚醯亞胺膜之L值為28~45。 [1] A polyimide film with a thickness of 1.0~10.0μm, characterized in that: when the molecular weight of the repeating unit of the polyimide is set to 100%, the molecular weight of the imine group is 40% or less, and The L value of polyimide film is 28~45.

〔2〕如上述〔1〕之聚醯亞胺膜,其中聚醯亞胺膜係藉由膜之機械搬送方向(MD)與寬度方向(TD)之雙軸延伸處理而延伸,且膜之總延伸倍率(MD之延伸倍率×TD之延伸倍率)為1.60以上。 [2] The polyimide film as described in [1] above, wherein the polyimide film is stretched by biaxial stretching in the mechanical transport direction (MD) and the width direction (TD) of the film, and the total film Stretching ratio (MD stretching ratio×TD stretching ratio) is 1.60 or more.

〔3〕如上述〔1〕~〔2〕中任一項之聚醯亞胺膜,其係由芳香族二胺成分為選自由對苯二胺、4,4'-二胺基二苯基醚及3,4'-二胺基二苯基醚所組成之群中之1種以上,芳香族酸酐成分為苯均四酸二酐及/或3,3',4,4'-聯苯四羧酸二酐之聚醯胺酸所製造。 [3] The polyimide film of any one of [1] to [2] above, which is composed of aromatic diamine components selected from p-phenylenediamine, 4,4'-diaminodiphenyl One or more of the group consisting of ether and 3,4'-diaminodiphenyl ether, the aromatic anhydride component is pyromellitic dianhydride and/or 3,3',4,4'-biphenyl Manufactured by polyamide acid of tetracarboxylic dianhydride.

〔4〕如上述〔1〕~〔3〕中任一項之聚醯亞胺膜之製造方法,其將可形成聚醯亞胺膜之凝膠膜進行延伸而獲得之膜於350~500℃下進行5~300秒鐘之加熱處理,上述聚醯亞胺膜係將聚醯亞胺之重複單元之分子量設為100%時,其醯亞胺基之分子量為40%以下者。 [4] The polyimide film manufacturing method as described in any one of [1] to [3] above, which stretches the gel film that can form the polyimide film to obtain a film at 350~500℃ Heat treatment for 5 to 300 seconds. When the polyimide film has a molecular weight of 100% of the repeating unit of the polyimide film, the molecular weight of the polyimide group is less than 40%.

〔5〕一種聚醯亞胺膜,其特徵在於:包含如上述〔1〕~〔4〕中任一項之聚醯亞胺膜(A)、及積層於聚醯亞胺膜(A)之單面或者兩面上之聚醯亞胺膜(B)。 [5] A polyimide film, characterized in that it comprises the polyimide film (A) as described in any one of [1] to [4] above, and a layer laminated on the polyimide film (A) Polyimide film on one or both sides (B).

〔6〕如上述〔1〕~〔5〕中任一項之聚醯亞胺膜,其中聚醯亞胺膜之形態為寬度500~3000mm、長度1000m以上之聚醯亞胺膜捲。 [6] The polyimide film according to any one of [1] to [5] above, wherein the form of the polyimide film is a polyimide film roll with a width of 500-3000 mm and a length of 1000 m or more.

根據本發明,可獲得一種厚度為1.0~10.0μm、即便浸漬於鹼性溶液中亦不易發生由膜之變質及/或水解所導致之特性劣化、耐鹼性優異之聚醯亞胺膜。 According to the present invention, it is possible to obtain a polyimide film with a thickness of 1.0 to 10.0 μm, which is less prone to deterioration in characteristics caused by film deterioration and/or hydrolysis even when immersed in an alkaline solution, and is excellent in alkali resistance.

又,根據本發明,可獲得一種於製膜步驟中之膜之破損或皺褶經減少之製膜穩定性優異、厚度為1.0~10.0μm之聚醯亞胺膜。 In addition, according to the present invention, a polyimide film with a thickness of 1.0 to 10.0 μm can be obtained in which the damage or wrinkles of the film in the film forming step are reduced and the film forming stability is excellent.

進而,根據本發明,可獲得一種厚度為1.0~10.0μm、耐鹼性優異、於FPC製造步驟中之乾抗蝕膜之剝離步驟中由斷裂強度之降低或裂縫等所引起之故障較少的聚醯亞胺膜。 Furthermore, according to the present invention, it is possible to obtain a product having a thickness of 1.0 to 10.0 μm, excellent alkali resistance, and less failure caused by a decrease in breaking strength or cracks in the peeling step of the dry resist film in the FPC manufacturing step Polyimide film.

以下,對本發明進行具體說明。 Hereinafter, the present invention will be described in detail.

本發明之聚醯亞胺膜之厚度通常為1.0~10.0μm,較佳為2.0~9.0μm,更佳為3.0~8.0μm。 The thickness of the polyimide film of the present invention is usually 1.0 to 10.0 μm, preferably 2.0 to 9.0 μm, and more preferably 3.0 to 8.0 μm.

本發明之聚醯亞胺膜之L值通常為28~45,較佳為28~44,更佳為29~43,進而較佳為30~42。 The L value of the polyimide film of the present invention is usually 28-45, preferably 28-44, more preferably 29-43, and still more preferably 30-42.

L值可藉由選擇聚醯亞胺之構成成分或其比例、聚醯胺酸膜(凝膠膜)之處理條件(熱處理條件、延伸條件)等而調整。 The L value can be adjusted by selecting the constituent components of the polyimide or the ratio thereof, the processing conditions (heat treatment conditions, stretching conditions) of the polyimide film (gel film), and the like.

例如,對於凝膠膜,如後述般進行熱處理,但由於藉由選擇此種熱處理條件(溫度、時間等)而可調整聚醯亞胺之結晶化或結構變化之程度、進而可調整膜表面之氧化程度,故而可調整膜之L值。 For example, for a gel film, heat treatment is performed as described later, but by selecting such heat treatment conditions (temperature, time, etc.), the degree of crystallization or structural change of polyimide can be adjusted, and the film surface can be adjusted. The degree of oxidation can adjust the L value of the film.

再者,作為藉由選擇如上所述之特定範圍之L值而可獲得耐鹼性(進一步而言為製膜穩定性)優異之膜的理由之一,例如可想到如下理由。 Furthermore, as one of the reasons why a film excellent in alkali resistance (more specifically, film forming stability) can be obtained by selecting the L value in the specific range as described above, for example, the following reasons are conceivable.

藉由強化對凝膠膜之熱處理,伴隨著聚合物鏈之再排列或交聯結構之形成而促進結晶化,進而L值變低。如此,隨著膜表面之吸水性提高,耐鹼性亦提高。而且,藉由進而將結晶化之進行設為適當之(即,L值不過低)範圍,可擔保製造步驟時之膜之強度及柔軟性,可高效率地兼具耐鹼性與優異之製膜穩定性。 By strengthening the heat treatment of the gel film, the crystallization is promoted along with the rearrangement of polymer chains or the formation of a cross-linked structure, and the L value becomes lower. In this way, as the water absorption of the film surface increases, the alkali resistance also increases. Moreover, by further setting the progress of crystallization to an appropriate range (that is, the L value is not too low), the strength and flexibility of the film during the manufacturing step can be guaranteed, and the alkali resistance and excellent manufacturing can be efficiently combined Membrane stability.

若L值為如上所述之範圍,則即便聚醯亞胺膜之厚度薄至1.0~10.0μm,亦耐鹼性優異,故較佳。又,若為此範圍,則即便目標聚醯亞胺膜之厚度薄至1.0~10.0μm,亦於聚醯亞胺膜之製造步驟中減少膜之破損或皺褶之產生,製膜穩定性優異,故較佳。 If the L value is in the above-mentioned range, even if the thickness of the polyimide film is as thin as 1.0 to 10.0 μm, it is excellent in alkali resistance, which is preferable. In addition, if the range is within this range, even if the thickness of the target polyimide film is as thin as 1.0~10.0μm, the film breakage or wrinkles are reduced during the production process of the polyimide film, and the film formation stability is excellent , So better.

再者,L值係藉由後述實施例中記載之方法而測定之值。L值可 藉由重疊聚醯亞胺膜並將總厚設為50~60μm而測定。 In addition, L value is the value measured by the method described in the Example mentioned later. L value can It is measured by overlapping polyimide films and setting the total thickness to 50-60 μm.

本發明之聚醯亞胺膜於將聚醯亞胺之重複單元之分子量設為100%時,下述式(1)所表示之醯亞胺基之分子量通常為40%以下,較佳為39%以下,更佳為38%以下。 In the polyimide film of the present invention, when the molecular weight of the repeating unit of the polyimine is set to 100%, the molecular weight of the imine group represented by the following formula (1) is usually 40% or less, preferably 39 % Or less, more preferably 38% or less.

再者,「聚醯亞胺之重複單元之分子量」及「聚醯亞胺之分子量」為相同含義。 Furthermore, "the molecular weight of the repeating unit of polyimine" and "the molecular weight of polyimine" have the same meaning.

若為此種範圍,則聚醯亞胺膜之耐鹼性提高,故較佳。可認為,聚醯亞胺膜中,醯亞胺基之含量越多,吸水性變得越高。另一方面可認為,醯亞胺基以外之疏水成分之含量越多,聚醯亞胺膜之吸水性越降低,耐鹼性越提高。 If it is in this range, the alkali resistance of the polyimide film is improved, which is preferable. It can be considered that the higher the content of the imine group in the polyimide film, the higher the water absorption. On the other hand, it can be considered that the higher the content of hydrophobic components other than the imine group, the lower the water absorption of the polyimide film and the higher the alkali resistance.

Figure 105107078-A0202-12-0006-1
Figure 105107078-A0202-12-0006-1

又,本發明之聚醯亞胺膜之寬度並無特別限定,較佳為500~3000mm,更佳為1000~2800mm,進而較佳為1500~2500mm。 Furthermore, the width of the polyimide film of the present invention is not particularly limited, and is preferably 500 to 3000 mm, more preferably 1000 to 2800 mm, and still more preferably 1500 to 2500 mm.

又,本發明之聚醯亞胺膜之長度並無特別限定,較佳為1000m以上,更佳為2000~50000m,進而較佳為3000~30000m。 In addition, the length of the polyimide film of the present invention is not particularly limited, but is preferably 1,000 m or more, more preferably 2,000 to 50,000 m, and still more preferably 3,000 to 30,000 m.

[聚醯胺酸] [Polyamide acid]

於獲得本發明之聚醯亞胺膜時,首先使芳香族二胺成分及芳香族酸酐成分於有機溶劑中聚合,藉此獲得聚醯胺酸溶液(以下亦稱為聚醯胺酸溶液)。以下,對聚醯胺酸溶液進行說明。 To obtain the polyimide film of the present invention, first, the aromatic diamine component and the aromatic acid anhydride component are polymerized in an organic solvent to obtain a polyimide acid solution (hereinafter also referred to as polyimide acid solution). Hereinafter, the polyamide acid solution will be described.

本發明中,聚醯胺酸溶液可藉由使原料之芳香族二胺成分與芳香族酸酐成分、或以此兩者為主成分之化學物質於有機溶劑中聚合而獲得。 In the present invention, the polyamide acid solution can be obtained by polymerizing the aromatic diamine component and the aromatic anhydride component, or a chemical substance containing the two as main components, in an organic solvent.

作為芳香族二胺成分,例如可列舉:對苯二胺、間苯二胺、聯苯胺、對苯二甲胺、4,4'-二胺基二苯基醚、3,4'-二胺基二苯基醚、4,4'-二胺基二苯基甲烷、4,4'-二胺基二苯基碸、3,3'-二甲基-4,4'-二胺基二苯基甲烷、1,5-二胺基萘、3,3'-二甲氧基聯苯胺、1,4-雙(3-甲基-5-胺基苯基)苯及該等之醯胺形成性衍生物。該等可單獨使用1種,亦可將2種以上混合使用。 Examples of aromatic diamine components include p-phenylenediamine, m-phenylenediamine, benzidine, p-xylylenediamine, 4,4'-diaminodiphenyl ether, 3,4'-diamine Diphenyl ether, 4,4'-diaminodiphenylmethane, 4,4'-diaminodiphenylmethane, 3,3'-dimethyl-4,4'-diaminodi Phenylmethane, 1,5-diaminonaphthalene, 3,3'-dimethoxybenzidine, 1,4-bis(3-methyl-5-aminophenyl)benzene and these amides Formative derivatives. These may be used individually by 1 type, and may mix and use 2 or more types.

作為芳香族二胺成分,就所獲得之聚醯亞胺膜於低熱膨脹性及柔韌性方面優異等觀點而言,較佳為選自由對苯二胺、4,4'-二胺基二苯基醚及3,4'-二胺基二苯基醚所組成之群中之1種以上,更佳為對苯二胺與4,4'-二胺基二苯基醚之組合。 The aromatic diamine component is preferably selected from the group consisting of p-phenylenediamine and 4,4'-diaminodiphenyl from the viewpoint of the obtained polyimide film being excellent in low thermal expansion and flexibility, etc. One or more of the group consisting of phenylether and 3,4'-diaminodiphenyl ether, and more preferably a combination of p-phenylenediamine and 4,4'-diaminodiphenyl ether.

本發明中,作為用於形成聚醯胺酸溶液之原料,亦可於不妨礙本發明之效果之範圍內包含上述芳香族二胺成分以外之其他二胺成分。 In the present invention, as a raw material for forming a polyamide acid solution, other diamine components other than the above-mentioned aromatic diamine components may be contained within a range that does not hinder the effects of the present invention.

作為上述其他二胺成分,例如可列舉:3,3'-二胺基二苯基醚、間苯二胺、4,4'-二胺基二苯基丙烷、3,4'-二胺基二苯基丙烷、3,3'-二胺基二苯基丙烷、4,4'-二胺基二苯基甲烷、3,4'-二胺基二苯基甲烷、3,3'-二胺基二苯基甲烷、聯苯胺、4,4'-二胺基二苯基硫醚、3,4'-二胺基二苯基硫醚、3,3'-二胺基二苯基硫醚、4,4'-二胺基二苯基碸、3,4'-二胺基二苯基碸、3,3'-二胺基二苯基碸、2,6-二胺基吡啶、雙-(4-胺基苯基)二乙基矽烷、3,3'-二氯聯苯胺、雙-(4-胺基苯基)乙基氧化膦、雙-(4-胺基苯基)苯基氧化膦、雙-(4-胺基苯基)-N-苯基胺、雙-(4-胺基苯基)-N-甲基胺、1,5-二胺基萘、3,3'-二甲基-4,4'-二胺基聯苯、3,4'-二甲基-3',4-二胺基聯苯-3,3'-二甲氧基聯苯胺、2,4-雙(對-β-胺基-第三丁基苯基)醚、雙(對-β-胺基-第三丁基苯基)醚、對雙(2-甲基-4-胺戊基)苯、對雙-(1,1-二甲基-5-胺基戊基)苯、間苯二甲胺、對苯二甲胺、1,3-二胺基金剛烷、3,3'-二胺基-1,1'-二胺基金剛烷、3,3'-二胺基 甲基-1,1'-二金剛烷、雙(對胺基環己基)甲烷、六亞甲基二胺、七亞甲基二胺、八亞甲基二胺、九亞甲基二胺、十亞甲基二胺、3-甲基七亞甲基二胺、4,4'-二甲基七亞甲基二胺、2,11-二胺基十二烷、1,2-雙(3-胺基丙氧基)乙烷、2,2-二甲基丙二胺、3-甲氧基六伸乙基二胺、2,5-二甲基六亞甲基二胺、2,5-二甲基七亞甲基二胺、5-甲基九亞甲基二胺、1,4-二胺基環己烷、1,12-二胺基十八烷、2,5-二胺基-1,3,4-

Figure 105107078-A0202-12-0008-3
二唑、2,2-雙(4-胺基苯基)六氟丙烷、N-(3-胺基苯基)-4-胺基苯甲醯胺、4-胺基苯基-3-胺基苯甲酸酯等。該等可單獨使用1種,亦可將2種以上混合使用。 Examples of the above-mentioned other diamine components include: 3,3'-diaminodiphenyl ether, m-phenylenediamine, 4,4'-diaminodiphenylpropane, 3,4'-diamino Diphenylpropane, 3,3'-diaminodiphenylpropane, 4,4'-diaminodiphenylmethane, 3,4'-diaminodiphenylmethane, 3,3'-di Amino diphenylmethane, benzidine, 4,4'-diaminodiphenyl sulfide, 3,4'-diaminodiphenyl sulfide, 3,3'-diaminodiphenyl sulfide Ether, 4,4'-diaminodiphenyl sulfide, 3,4'-diaminodiphenyl sulfide, 3,3'-diaminodiphenyl sulfide, 2,6-diaminopyridine, Bis-(4-aminophenyl)diethylsilane, 3,3'-dichlorobenzidine, bis-(4-aminophenyl)ethyl phosphine oxide, bis-(4-aminophenyl) Phenylphosphine oxide, bis-(4-aminophenyl)-N-phenylamine, bis-(4-aminophenyl)-N-methylamine, 1,5-diaminonaphthalene, 3, 3'-dimethyl-4,4'-diaminobiphenyl, 3,4'-dimethyl-3',4-diaminobiphenyl-3,3'-dimethoxybenzidine, 2,4-bis(p-β-amino-tertiary butylphenyl) ether, bis(p-β-amino-tertiary butylphenyl) ether, p-bis(2-methyl-4- Aminopentyl)benzene, p-bis-(1,1-dimethyl-5-aminopentyl)benzene, m-xylylenediamine, p-xylylenediamine, 1,3-diamine pyridine, 3 ,3'-Diamino-1,1'-Diamine Fundmantane, 3,3'-Diaminomethyl-1,1'-Diadamantane, Bis(p-aminocyclohexyl)methane, Hexa Methylene diamine, heptamethylene diamine, octamethylene diamine, nonamethylene diamine, decamethylene diamine, 3-methyl heptamethylene diamine, 4,4'- Dimethylheptamethylene diamine, 2,11-diaminododecane, 1,2-bis(3-aminopropoxy)ethane, 2,2-dimethylpropanediamine, 3 -Methoxyhexamethylene diamine, 2,5-dimethylhexamethylene diamine, 2,5-dimethylheptamethylene diamine, 5-methylnonamethylene diamine, 1,4-diaminocyclohexane, 1,12-diaminooctadecane, 2,5-diamino-1,3,4-
Figure 105107078-A0202-12-0008-3
Diazole, 2,2-bis(4-aminophenyl)hexafluoropropane, N-(3-aminophenyl)-4-aminobenzamide, 4-aminophenyl-3-amine Base benzoate and so on. These may be used individually by 1 type, and may mix and use 2 or more types.

作為上述芳香族酸酐成分之具體例,例如可列舉:苯均四酸、3,3',4,4'-聯苯四羧酸、2,3',3,4'-聯苯四羧酸、3,3',4,4'-二苯甲酮四羧酸、2,3,6,7-萘四羧酸、2,2-雙(3,4-二羧基苯基)醚、吡啶-2,3,5,6-四羧酸及該等之醯胺形成性衍生物等芳香族四羧酸酐成分。該等可單獨使用1種,亦可將2種以上混合使用。 Specific examples of the above-mentioned aromatic acid anhydride components include, for example, pyromellitic acid, 3,3',4,4'-biphenyltetracarboxylic acid, 2,3',3,4'-biphenyltetracarboxylic acid , 3,3',4,4'-benzophenone tetracarboxylic acid, 2,3,6,7-naphthalene tetracarboxylic acid, 2,2-bis(3,4-dicarboxyphenyl) ether, pyridine -2,3,5,6-tetracarboxylic acid and aromatic tetracarboxylic anhydride components such as amide-forming derivatives. These may be used individually by 1 type, and may mix and use 2 or more types.

作為芳香族酸酐成分,就所獲得之聚醯亞胺膜於耐熱性及低吸水性方面優異等觀點而言,較佳為選自由苯均四酸二酐及3,3',4,4'-聯苯四羧酸二酐所組成之群中之1種以上。 The aromatic acid anhydride component is preferably selected from the group consisting of pyromellitic dianhydride and 3,3',4,4' from the viewpoint of the obtained polyimide film being excellent in heat resistance and low water absorption. -One or more of the group consisting of biphenyltetracarboxylic dianhydride.

本發明中,作為用於形成聚醯胺酸溶液之原料,亦可於不損及本發明之效果之範圍內包含上述芳香族酸酐成分以外之其他酸酐成分。 In the present invention, as a raw material for forming a polyamide acid solution, an acid anhydride component other than the above-mentioned aromatic acid anhydride component may be contained within a range that does not impair the effects of the present invention.

作為上述其他酸酐成分,例如可列舉:2,3',3,4'-聯苯四羧酸二酐、3,3',4,4'-二苯甲酮四羧酸二酐、2,3,6,7-萘二羧酸二酐、2,2-雙(3,4-二羧基苯基)醚、吡啶-2,3,5,6-四羧酸二酐、1,2,4,5-萘四羧酸二酐、1,4,5,8-萘四羧酸二酐、1,4,5,8-十氫萘四羧酸二酐、4,8-二甲基-1,2,5,6-六氫萘四羧酸二酐、2,6-二氯-1,4,5,8-萘四羧酸二酐、2,7-二氯-1,4,5,8-萘四羧酸二酐、2,3,6,7-四氯-1,4,5,8-萘四羧酸二酐、1,8,9,10- 菲四羧酸二酐、2,2-雙(2,3-二羧基苯基)丙烷二酐、1,1-雙(3,4-二羧基苯基)乙烷二酐、1,1-雙(2,3-二羧基苯基)乙烷二酐、雙(2,3-二羧基苯基)甲烷二酐、雙(3,4-二羧基苯基)甲烷二酐、雙(3,4-二羧基苯基)碸二酐、苯-1,2,3,4-四羧酸二酐、3,4,3',4'-二苯甲酮四羧酸二酐等。該等可單獨使用1種,亦可將2種以上混合使用。 Examples of the above-mentioned other acid anhydride components include: 2,3',3,4'-biphenyltetracarboxylic dianhydride, 3,3',4,4'-benzophenonetetracarboxylic dianhydride, 2, 3,6,7-naphthalene dicarboxylic dianhydride, 2,2-bis(3,4-dicarboxyphenyl) ether, pyridine-2,3,5,6-tetracarboxylic dianhydride, 1, 2, 4,5-naphthalenetetracarboxylic dianhydride, 1,4,5,8-naphthalenetetracarboxylic dianhydride, 1,4,5,8-decahydronaphthalenetetracarboxylic dianhydride, 4,8-dimethyl -1,2,5,6-hexahydronaphthalenetetracarboxylic dianhydride, 2,6-dichloro-1,4,5,8-naphthalenetetracarboxylic dianhydride, 2,7-dichloro-1,4 ,5,8-Naphthalenetetracarboxylic dianhydride, 2,3,6,7-tetrachloro-1,4,5,8-naphthalenetetracarboxylic dianhydride, 1,8,9,10- Phenanthrene tetracarboxylic dianhydride, 2,2-bis(2,3-dicarboxyphenyl)propane dianhydride, 1,1-bis(3,4-dicarboxyphenyl)ethane dianhydride, 1,1- Bis(2,3-dicarboxyphenyl)ethane dianhydride, bis(2,3-dicarboxyphenyl)methane dianhydride, bis(3,4-dicarboxyphenyl)methane dianhydride, bis(3, 4-Dicarboxyphenyl) bismuth dianhydride, benzene-1,2,3,4-tetracarboxylic dianhydride, 3,4,3',4'-benzophenone tetracarboxylic dianhydride, etc. These may be used individually by 1 type, and may mix and use 2 or more types.

本發明中,作為特別佳之芳香族二胺成分及芳香族酸酐成分之組合,就所獲得之聚醯亞胺膜於耐熱性、低吸水性、低熱膨脹性及柔韌性方面優異等觀點而言,可列舉:作為芳香族二胺成分之4,4'-二胺基二苯基醚、或對苯二胺與4,4'-二胺基二苯基醚,與作為芳香族酸酐成分之苯均四酸二酐、或苯均四酸二酐與3,3',4,4'-聯苯四羧酸二酐之組合。其中,尤佳為4,4'-二胺基二苯基醚與苯均四酸二酐之組合。 In the present invention, as a particularly preferable combination of an aromatic diamine component and an aromatic acid anhydride component, from the viewpoints that the obtained polyimide film is excellent in heat resistance, low water absorption, low thermal expansion, and flexibility, etc. Examples include: 4,4'-diaminodiphenyl ether as an aromatic diamine component, or p-phenylenediamine and 4,4'-diaminodiphenyl ether, and benzene as an aromatic anhydride component Pyromellitic dianhydride, or a combination of pyromellitic dianhydride and 3,3',4,4'-biphenyltetracarboxylic dianhydride. Among them, a combination of 4,4'-diaminodiphenyl ether and pyromellitic dianhydride is particularly preferred.

本發明中,對苯二胺與4,4'-二胺基二苯基醚之莫耳比較佳為40/60~0/100,更佳為30/70~0/100。 In the present invention, the molar ratio of p-phenylenediamine and 4,4'-diaminodiphenyl ether is preferably 40/60~0/100, more preferably 30/70~0/100.

本發明中,苯均四酸二酐與3,3',4,4'-聯苯四羧酸二酐之莫耳比較佳為100/0~40/60,更佳為100/0~65/35。 In the present invention, the molar ratio of pyromellitic dianhydride and 3,3',4,4'-biphenyltetracarboxylic dianhydride is preferably 100/0~40/60, more preferably 100/0~65 /35.

又,本發明中,作為用於形成聚醯胺酸溶液之有機溶劑之具體例,例如可列舉;二甲基亞碸、二乙基亞碸等亞碸系溶劑;N,N-二甲基甲醯胺、N,N-二乙基甲醯胺等甲醯胺系溶劑;N,N-二甲基乙醯胺、N,N-二乙基乙醯胺等乙醯胺系溶劑;N-甲基-2-吡咯啶酮、N-乙烯基-2-吡咯啶酮等吡咯啶酮系溶劑;苯酚、鄰甲酚、間甲酚或對甲酚、二甲苯酚、鹵化苯酚、鄰苯二酚等酚系溶劑;六甲基磷醯胺、γ-丁內酯等非質子性極性溶劑等。該等可單獨使用,或將2種以上組合使用,進而可與二甲苯、甲苯等芳香族烴組合使用。 Furthermore, in the present invention, specific examples of the organic solvent used to form the polyamide acid solution include, for example, sulfinous solvents such as dimethyl sulfene and diethyl sulfin; N,N-dimethyl Formamide solvents such as formamide and N,N-diethylformamide; acetamide solvents such as N,N-dimethylacetamide and N,N-diethylacetamide; N -Methyl-2-pyrrolidone, N-vinyl-2-pyrrolidone and other pyrrolidone solvents; phenol, o-cresol, m-cresol or p-cresol, xylenol, halogenated phenol, o-benzene Phenolic solvents such as diphenols; aprotic polar solvents such as hexamethylphosphamide and γ-butyrolactone. These can be used alone or in combination of two or more, and can be used in combination with aromatic hydrocarbons such as xylene and toluene.

聚醯胺酸溶液之聚合方法可藉由公知之任一方法而進行,例如可列舉下述方法。 The polymerization method of the polyamide acid solution can be carried out by any known method, for example, the following methods can be mentioned.

(1)首先將芳香族二胺成分總量放入至溶劑中,然後以與芳香族 二胺成分總量成為等量之方式加入芳香族酸酐成分而進行聚合之方法。 (1) First put the total amount of aromatic diamine components into the solvent, and then combine with the aromatic diamine The total amount of diamine components is a method in which aromatic acid anhydride components are added in an equal amount to perform polymerization.

(2)首先將芳香族酸酐成分總量放入至溶劑中,然後以與芳香族酸酐成分成為等量之方式加入芳香族二胺成分而進行聚合之方法。 (2) A method in which the total amount of aromatic acid anhydride components is first put into a solvent, and then the aromatic diamine component is added in an equivalent amount to the aromatic acid anhydride component to perform polymerization.

(3)將一部分芳香族二胺成分放入至溶劑中後,以相對於反應成分而一部分芳香族酸酐成分成為95~105莫耳%之比率以反應所需之時間混合後,添加另一部分芳香族二胺成分,繼而以所有芳香族二胺成分與所有芳香族酸酐成分成大致等量之方式添加另一部分芳香族酸酐成分而進行聚合之方法。 (3) After putting a part of the aromatic diamine component in the solvent, the part of the aromatic acid anhydride component is 95~105 mol% relative to the reaction component, and after mixing for the time required for the reaction, add another part of the aromatic A method in which all the aromatic diamine components and all the aromatic acid anhydride components are then added in such a way that all of the aromatic diamine components and all the aromatic acid anhydride components are substantially equal to each other to carry out polymerization.

(4)將一部分芳香族酸酐成分放入至溶劑中後,以相對於反應成分而一部分芳香族二胺成分成為95~105莫耳%之比率以反應所需之時間混合後,添加另一部分芳香族酸酐成分,繼而以所有芳香族二胺成分與所有芳香族酸酐成分成為大致等量之方式添加另一部分芳香族二胺成分而進行聚合之方法。 (4) After putting a part of the aromatic acid anhydride component in the solvent, the ratio of the part of the aromatic diamine component to the reaction component is 95~105 mol% after mixing for the time required for the reaction, and then adding another part of the aromatic A method of polymerization by adding another part of the aromatic diamine component so that all the aromatic diamine components and all the aromatic acid anhydride components become approximately equal amounts.

(5)於溶劑中使一部分芳香族二胺成分與芳香族酸酐成分以任一者成為過量之方式反應而製備聚醯胺酸溶液(A),於其他溶劑中使另一部分芳香族二胺成分與芳香族酸酐成分以任一者成為過量之方式反應而製備聚醯胺酸溶液(B)。將如此獲得之各聚醯胺酸溶液(A)與(B)混合,完成聚合之方法。此時,於製備聚醯胺酸溶液(A)時芳香族二胺成分過量之情形時,於聚醯胺酸溶液(B)中使芳香族酸酐成分過量,又,於聚醯胺酸溶液(A)中芳香族酸酐成分過量之情形時,於聚醯胺酸溶液(B)中使芳香族二胺成分過量,混合聚醯胺酸溶液(A)與(B),以該等用於反應之所有芳香族二胺成分所有全芳香族酸酐成分成為大致等量之方式製備之方法等。 (5) A part of the aromatic diamine component and the aromatic anhydride component are reacted in a solvent such that either one becomes excessive to prepare a polyamide acid solution (A), and another part of the aromatic diamine component is made in another solvent It reacts with an aromatic acid anhydride component so that any one becomes excessive, and the polyamide acid solution (B) is prepared. The polyamic acid solutions (A) and (B) thus obtained are mixed to complete the polymerization method. At this time, when the aromatic diamine component is excessive in the preparation of the polyamide acid solution (A), the aromatic acid anhydride component is excessive in the polyamide acid solution (B), and the polyamide acid solution ( When the aromatic acid anhydride component is excessive in A), make the aromatic diamine component excessive in the polyamic acid solution (B), mix the polyamic acid solution (A) and (B), and use them for the reaction All aromatic diamine components and all fully aromatic anhydride components are prepared in roughly equal amounts.

再者,聚合方法並不限定於此,亦可使用其他公知之方法。 In addition, the polymerization method is not limited to this, and other known methods may be used.

本發明中構成聚醯胺酸之芳香族酸酐成分與芳香族二胺成分係 以各自之莫耳數成為大致相等之比例而聚合,其中一者亦可於例如10莫耳%、較佳為5莫耳%之範圍內相對於另一者而過量調配。 In the present invention, the aromatic acid anhydride component and the aromatic diamine component constituting the polyamide acid are It is polymerized so that the respective molar numbers become approximately equal proportions, and one of them may be over-adjusted relative to the other in the range of, for example, 10 mol%, preferably 5 mol%.

聚合反應較佳為於一面有機溶劑中攪拌一面進行。聚合溫度並無特別限定,通常以反應溶液之內溫0~80℃進行。聚合時間並無特別限定,較佳為連續進行10分鐘~30小時。聚合反應可根據需要而分割聚合反應、或使溫度上升下降。兩反應體之添加順序並無特別限制,較佳為於芳香族二胺成分之溶液中添加芳香族酸酐。於製造優質之聚醯胺酸之有機溶劑溶液方面而言,於聚合反應中進行真空消泡係有效之方法。又,藉由在聚合反應之前於芳香族二胺類中添加少量之封端劑,亦可控制聚合反應。上述封端劑並無特別限定,可使用公知者。 The polymerization reaction is preferably carried out while stirring in an organic solvent. The polymerization temperature is not particularly limited, and it is usually carried out at the internal temperature of the reaction solution from 0 to 80°C. The polymerization time is not particularly limited, but it is preferably continuously performed for 10 minutes to 30 hours. The polymerization reaction may be divided into sections or the temperature may be increased or decreased as necessary. The order of addition of the two reactants is not particularly limited, but it is preferable to add an aromatic anhydride to the solution of the aromatic diamine component. In terms of producing high-quality organic solvent solutions of polyamide acid, vacuum defoaming during polymerization is an effective method. Furthermore, by adding a small amount of a blocking agent to the aromatic diamines before the polymerization reaction, the polymerization reaction can also be controlled. The said blocking agent is not specifically limited, A well-known thing can be used.

如此獲得之聚醯胺酸溶液通常包含5~40重量%、較佳為10~30重量%之固形物成分。又,其黏度係利用布氏黏度計而獲得之測定值,並無特別限定,通常為10~2000Pa‧s,為了實現穩定之輸液,較佳為100~1000Pa‧s。再者,有機溶劑溶液中之聚醯胺酸亦可局部地經醯亞胺化。 The polyamide acid solution thus obtained usually contains 5-40% by weight, preferably 10-30% by weight of solid content. In addition, the viscosity is a measured value obtained by using a Brookfield viscometer, and is not particularly limited. It is usually 10~2000Pa‧s. In order to achieve stable infusion, it is preferably 100~1000Pa‧s. Furthermore, the polyamic acid in the organic solvent solution can also be partially imidized.

又,上述聚醯胺酸溶液視需要可含有氧化鈦、氧化矽、碳酸鈣、磷酸鈣、磷酸氫鈣以及聚醯亞胺填料等化學上非活性之有機填料或無機填料。填料之含量只要不損及本發明之效果則並無特別限定。 In addition, the polyamide acid solution may contain chemically inactive organic or inorganic fillers such as titanium oxide, silicon oxide, calcium carbonate, calcium phosphate, calcium hydrogen phosphate, and polyimide fillers as needed. The content of the filler is not particularly limited as long as it does not impair the effect of the present invention.

此處所使用之聚醯胺酸溶液可為預先聚合而成之聚醯胺酸溶液,亦可為於含有填料粒子時依序聚合而成者。 The polyamide acid solution used here may be a polyamide acid solution prepared by polymerization in advance, or may be a polyamide acid solution obtained by sequential polymerization when it contains filler particles.

又,上述聚醯胺酸溶液亦可含有1種或2種以上之上述填料以外之化合物。作為填料以外之化合物,例如可列舉碳、氧化鋁或二氧化鈦等金屬氧化物、氮化硼等硼化合物等。 In addition, the polyamide acid solution may contain one or more compounds other than the filler. Examples of compounds other than fillers include metal oxides such as carbon, aluminum oxide or titanium dioxide, and boron compounds such as boron nitride.

以下,對本發明之聚醯亞胺膜之製造方法進行說明。 Hereinafter, the manufacturing method of the polyimide film of the present invention will be described.

本發明之聚醯亞胺膜係藉由將上述聚醯胺酸溶液加熱而製造, 以下將詳細記載。 The polyimide film of the present invention is produced by heating the above polyimide acid solution, It will be described in detail below.

作為製造聚醯亞胺膜之方法,可列舉:將聚醯胺酸溶液澆鑄為膜狀並進行熱脫環脫溶劑而獲得聚醯亞胺膜之方法;以及於聚醯胺酸溶液中混合環化觸媒及脫水劑進行化學脫環而製作凝膠膜,對其進行加熱脫溶劑,藉此獲得聚醯亞胺膜之方法;後者較佳。 As a method of manufacturing a polyimide film, there can be mentioned: a method of casting a polyimide acid solution into a film shape and thermally dering and removing the solvent to obtain a polyimide film; and mixing the ring in the polyimide acid solution The chemical catalyst and dehydrating agent are chemically decyclized to make a gel film, which is heated to remove the solvent to obtain a polyimide film; the latter is preferred.

於化學脫環之方法中,首先製備上述聚醯胺酸溶液。上述聚醯胺酸溶液可含有環化觸媒(醯亞胺化觸媒)、脫水劑以及凝膠化延遲劑等。 In the method of chemical decyclization, the above-mentioned polyamide acid solution is first prepared. The above-mentioned polyamide acid solution may contain a cyclization catalyst (imidation catalyst), a dehydrating agent, a gelation retarder, and the like.

作為本發明中所使用之環化觸媒之具體例,可列舉:三甲胺、三伸乙基二胺等脂肪族三級胺,二甲基苯胺等芳香族三級胺,以及異喹啉、吡啶、β-甲基吡啶等雜環式三級胺等,該等可單獨使用,或將2種以上併用。其中,較佳為使用至少1種以上之雜環式三級胺之態樣。 Specific examples of the cyclization catalyst used in the present invention include aliphatic tertiary amines such as trimethylamine and triethylenediamine, aromatic tertiary amines such as dimethylaniline, and isoquinoline, Heterocyclic tertiary amines such as pyridine and β-picoline can be used alone or in combination of two or more kinds. Among them, it is preferable to use at least one heterocyclic tertiary amine.

作為本發明中所使用之脫水劑之具體例,可列舉乙酸酐、丙酸酐、丁酸酐等脂肪族羧酸酐,以及苯甲酸酐等芳香族羧酸酐等,其中,較佳為乙酸酐及/或苯甲酸酐。 Specific examples of the dehydrating agent used in the present invention include aliphatic carboxylic anhydrides such as acetic anhydride, propionic anhydride, butyric anhydride, and aromatic carboxylic anhydrides such as benzoic anhydride. Among them, acetic anhydride and/or Benzoic anhydride.

作為由聚醯胺酸溶液製造聚醯亞胺膜之方法,將含有環化觸媒及脫水劑之聚醯胺酸溶液自附狹縫之噴嘴流延至支撐體上而成形為膜狀,於支撐體上局部進行醯亞胺化而製成具有自我支撐性之凝膠膜後,自支撐體剝離,進行加熱乾燥/醯亞胺化、熱處理。 As a method for producing polyimide film from polyamide acid solution, a polyimide acid solution containing a cyclization catalyst and a dehydrating agent is cast onto a support from a nozzle with a slit to be shaped into a film. After the body is partially imidized to form a self-supporting gel film, it is peeled off from the support, and is heated to dry/imide and heat treatment.

上述聚醯胺酸溶液係通過狹縫狀噴嘴而經成形為膜狀,流延至經加熱之支撐體上,於支撐體上進行熱閉環反應,成為具有自我支撐性之凝膠膜而自支撐體剝離。 The above-mentioned polyamide acid solution is formed into a film through a slit-shaped nozzle, and is cast on a heated support, and a thermal closed loop reaction is performed on the support to become a self-supporting gel film. Peel off.

所謂上述支撐體,為金屬製之轉筒或環帶,其溫度係藉由液體或氣體之熱媒、及/或電加熱器等之輻射熱而控制。 The above-mentioned support is a metal rotating drum or an endless belt, the temperature of which is controlled by a liquid or gas heat medium, and/or radiant heat from an electric heater.

上述凝膠膜藉由來自支撐體之受熱及/或來自熱風或電加熱器等 熱源之受熱,通常被加熱至30~200℃、較佳為40~150℃而進行閉環反應,使游離狀態之有機溶劑等揮發成分乾燥,由此變得具有自我支撐性,自支撐體剝離。此時,藉由使用存在於該支撐體表面之凹凸部分之直徑為10~100μm、凹凸部分之數量為每1cm2中為500~1500個、且凹凸部分之最大粗糙度為1~5μm的支撐體,而於10μm以下之薄聚醯亞胺膜之製造中亦可良好地剝離。 The above-mentioned gel film is heated to 30~200℃, preferably 40~150℃ by heating from the support and/or heating from the heat source such as hot air or electric heater. Volatile components such as organic solvents are dried to become self-supporting and peel off from the support. At this time, by using a support with a diameter of 10 to 100 μm in the concave and convex part existing on the surface of the support, the number of concave and convex parts is 500 to 1500 per 1 cm 2 , and the maximum roughness of the concave and convex part is 1 to 5 μm. It can also be peeled off well in the production of thin polyimide film of 10μm or less.

自上述支撐體剝離之凝膠膜通常藉由旋轉輥一面限制行進速度一面於行進方向上被延伸。行進方向上之延伸較佳為藉由旋轉輥以多階段進行。特別是10μm以下之薄聚醯亞胺膜之延伸中,藉由將旋轉輥設為S字包裹,或使用夾輥及吸輥以多階段控制張力,可防止膜之皺褶而更佳。行進方向上之延伸通常係於140℃以下之溫度下以1.01~1.90倍、較佳為1.05~1.60倍、進而較佳為1.10~1.50倍之倍率實施。於行進方向上經延伸之凝膠膜被導入至拉幅裝置中,由拉幅夾握持寬度方向兩端部,一面與拉幅夾一同行進,一面向寬度方向上延伸。 The gel film peeled from the above-mentioned support is usually stretched in the traveling direction by a rotating roller while restricting the traveling speed. The extension in the traveling direction is preferably performed in multiple stages by rotating rollers. Especially in the stretching of thin polyimide film below 10μm, it is better to prevent the film from wrinkles by setting the rotating roller as an S-wrap, or using nip rollers and suction rollers to control the tension in multiple stages. The extension in the traveling direction is usually performed at a temperature below 140° C. with a magnification of 1.01 to 1.90 times, preferably 1.05 to 1.60 times, and more preferably 1.10 to 1.50 times. The gel film stretched in the traveling direction is introduced into the tenter device, and the two ends in the width direction are held by the tenter clip, one side runs with the tenter clip, and the other side extends in the width direction.

關於凝膠膜之延伸,較佳為膜之總延伸倍率(膜之機械搬送方向(MD)之延伸倍率×寬度方向(TD)之延伸倍率)為1.60以上,更佳為1.70~3.00,進而較佳為1.80~2.60。若延伸倍率較高,則聚醯亞胺之分子鏈之配向性變高,故認為膜變得不易水解而耐鹼性提高,而較佳。 Regarding the extension of the gel film, it is preferable that the total extension ratio of the film (the extension ratio in the mechanical transport direction (MD) × the extension ratio in the width direction (TD)) of the film is 1.60 or more, more preferably 1.70~3.00, and more Preferably, it is 1.80~2.60. If the stretching ratio is higher, the alignment of the molecular chain of the polyimide becomes higher, so it is considered that the film becomes less hydrolyzed and the alkali resistance is improved, which is preferable.

可藉由調整上述MD之延伸倍率與TD之延伸倍率而調整聚醯亞胺膜之厚度。 The thickness of the polyimide film can be adjusted by adjusting the stretching ratio of MD and TD.

上述經延伸之凝膠膜通常係利用風、紅外線加熱器等加熱15秒鐘~30分鐘。繼而,藉由熱風及/或電加熱器等,通常以250~500℃之溫度進行5秒鐘~30分鐘之熱處理。熱處理溫度及時間可根據所獲得之聚醯亞胺膜之厚度而適當變更。 The stretched gel film is usually heated by wind, infrared heater, etc. for 15 seconds to 30 minutes. Then, with hot air and/or electric heaters, the heat treatment is usually performed at a temperature of 250 to 500°C for 5 seconds to 30 minutes. The heat treatment temperature and time can be appropriately changed according to the thickness of the obtained polyimide film.

熱處理溫度通常為250~500℃,較佳為300~500℃,更佳為350~500℃,進而較佳為370~490℃。 The heat treatment temperature is usually 250 to 500°C, preferably 300 to 500°C, more preferably 350 to 500°C, and still more preferably 370 to 490°C.

熱處理時間通常為5秒鐘~30分鐘,較佳為5秒鐘~20分鐘,更佳為5秒鐘~15分鐘,進而較佳為5秒鐘~300秒。 The heat treatment time is usually 5 seconds to 30 minutes, preferably 5 seconds to 20 minutes, more preferably 5 seconds to 15 minutes, and even more preferably 5 seconds to 300 seconds.

又,可藉由調整對凝膠膜進行熱處理時等之行進速度而調整聚醯亞胺膜之厚度。 In addition, the thickness of the polyimide film can be adjusted by adjusting the traveling speed during heat treatment of the gel film.

較佳為對如此而獲得之聚醯亞胺膜進而進行退火處理。退火處理之方法並無特別限定,只要依照常法即可。 It is preferable to further subject the polyimide film thus obtained to annealing treatment. The method of annealing treatment is not particularly limited, as long as it follows a common method.

作為退火處理之溫度,並無特別限定,較佳為200℃以上且600℃以下,更佳為200℃以上且550℃以下,特佳為210℃以上且500℃以下。具體而言,較佳為於經加熱至上述溫度範圍之爐中,以低張力使膜行進,進行退火處理。膜於爐中滯留之時間成為處理時間,藉由改變行進速度而對其進行控制,較佳為5秒鐘~5分鐘之處理時間。又,行進時之膜張力較佳為10~50N/m,更佳為20~30N/m。 The annealing temperature is not particularly limited, but is preferably 200°C or higher and 600°C or lower, more preferably 200°C or higher and 550°C or lower, and particularly preferably 210°C or higher and 500°C or lower. Specifically, it is preferable to perform annealing treatment by advancing the film under low tension in a furnace heated to the above-mentioned temperature range. The time the film stays in the furnace becomes the processing time, which is controlled by changing the traveling speed, preferably a processing time of 5 seconds to 5 minutes. Moreover, the film tension during travel is preferably 10-50 N/m, more preferably 20-30 N/m.

又,如上述般獲得之聚醯亞胺膜較佳為對膜表面實施大氣壓電漿或真空電漿表面處理等電漿表面處理。電漿表面處理之方法並無特別限定。 In addition, the polyimide film obtained as described above is preferably subjected to plasma surface treatment such as atmospheric piezoelectric plasma or vacuum plasma surface treatment on the surface of the film. The method of plasma surface treatment is not particularly limited.

本發明之聚醯亞胺膜之形態並無特別限定,較佳為捲狀。 The form of the polyimide film of the present invention is not particularly limited, and it is preferably a roll shape.

聚醯亞胺膜捲可藉由將聚醯亞胺膜捲繞至捲芯上而獲得。本發明中,捲繞至捲芯上之方法並無特別限定。 The polyimide film roll can be obtained by winding the polyimide film onto a roll core. In the present invention, the method of winding onto the core is not particularly limited.

作為上述捲芯之材質,並無特別限定,可使用先前公知者,例如可列舉:紙;氯乙烯等塑膠;由玻璃纖維與環氧樹脂、紙與酚樹脂、碳纖維與環氧樹脂等之組合等所形成之纖維強化塑膠(FRP);不鏽鋼等金屬;於紙製之芯中含浸樹脂而得者;或於該等之表面上形成樹脂層而得者等。 The material of the above-mentioned core is not particularly limited, and previously known materials can be used. Examples include: paper; plastics such as vinyl chloride; a combination of glass fiber and epoxy resin, paper and phenol resin, carbon fiber and epoxy resin, etc. Fiber reinforced plastics (FRP) formed by other materials; metals such as stainless steel; those obtained by impregnating resin in a paper core; or those obtained by forming a resin layer on the surface of such materials.

上述捲芯之直徑並無特別限定,例如為50~250mm,較佳為70 ~200mm。 The diameter of the core is not particularly limited, for example, 50~250mm, preferably 70 ~200mm.

藉由於如上述般獲得之本發明之聚醯亞胺膜(A)之單面或者兩面上塗佈作為聚醯亞胺之前驅物的聚醯胺酸之有機溶劑溶液,並對其進行加熱乾燥而積層聚醯亞胺膜(B),可獲得能夠用作FPC用基礎膜等之聚醯亞胺膜。該塗佈、加熱及乾燥方法並無特別限定。 The polyimide film (A) of the present invention obtained as described above is coated with an organic solvent solution of polyimide acid as a precursor of polyimide on one side or both sides, and heated and dried The laminated polyimide film (B) can obtain a polyimide film that can be used as a base film for FPC. The coating, heating, and drying methods are not particularly limited.

作為上述聚醯胺酸,例如可列舉:包含1,3-雙-(4-胺基苯氧基)苯與4,4'-二氧基二鄰苯二甲酸酐之聚醯胺酸、或包含2,2'-二甲基-4,4'-二胺基聯苯與苯均四酸二酐之聚醯胺酸等。聚醯胺酸可使用1種或2種以上。 As the above-mentioned polyamic acid, for example, polyamic acid containing 1,3-bis-(4-aminophenoxy)benzene and 4,4'-dioxydiphthalic anhydride, or Polyamide acid containing 2,2'-dimethyl-4,4'-diaminobiphenyl and pyromellitic dianhydride, etc. One type or two or more types of polyamide can be used.

作為上述有機溶劑,並無特別限定,例如可使用選自上文所述之可用於形成聚醯胺酸溶液之有機溶劑、可溶解熱塑性聚醯亞胺或聚醯胺酸之其他有機溶劑中之1種或2種以上等。 The above-mentioned organic solvent is not particularly limited. For example, it is possible to use one selected from the above-mentioned organic solvents that can be used to form polyamide acid solutions, and other organic solvents that can dissolve thermoplastic polyimide or polyamide acid. One type or two or more types, etc.

又,上述聚醯胺酸之有機溶劑溶液中,聚醯胺酸之固形物成分濃度並無特別限定,相對於該有機溶劑溶液總量,例如為10~30重量%。 In addition, in the organic solvent solution of the polyamide acid, the solid content concentration of the polyamide acid is not particularly limited, and is, for example, 10 to 30% by weight relative to the total amount of the organic solvent solution.

又,本發明之聚醯亞胺膜可用於FPC之基礎膜、電容器用絕緣膜、絕緣膠帶等用途中。 In addition, the polyimide film of the present invention can be used in applications such as a base film for FPC, an insulating film for capacitors, and an insulating tape.

[實施例] [Example]

以下,根據實施例對本發明進行說明,但本發明並不限定於該等實施例。又,上述記載及以下之實施例中闡述之各特性之評價方法以及評價基準如下所示。 Hereinafter, the present invention will be described based on examples, but the present invention is not limited to these examples. In addition, the evaluation methods and evaluation criteria of each characteristic explained in the above description and the following examples are as follows.

(1)斷裂強度及斷裂伸長率 (1) Breaking strength and breaking elongation

斷裂強度係設為根據JIS-K7113於室溫下藉由ORIENTEC公司製造之TENSILON型延伸試驗機,於300mm/分鐘之延伸速度下試樣斷裂時之強度及伸長率。試片之尺寸為10mm寬×250mm長,夾間距離係設為100mm,於25℃、60%RH之環境下進行測定。 The breaking strength is the strength and elongation when the sample breaks at an elongation speed of 300mm/min using a TENSILON type extension test machine manufactured by ORIENTEC at room temperature according to JIS-K7113. The size of the test piece is 10mm wide×250mm long, the distance between the clamps is set to 100mm, and the measurement is performed under an environment of 25°C and 60%RH.

(2)膜厚度 (2) Film thickness

重疊10片膜,使用SONY公司製造之數位式測微計M-30測定膜厚度,將其厚度值除以10而得之值之小數點第1位進行四捨五入,將所得之值作為膜厚度。 Overlap 10 films, measure the film thickness using a digital micrometer M-30 manufactured by SONY, and divide the thickness value by 10 to round to the first decimal place, and use the obtained value as the film thickness.

(3)膜L值 (3) Film L value

膜L值係使用SUGA TEST INSTRUMENTS製造之SM-7-CH而測定。將100mm×100mm之膜於膜寬度方向上分割成5份,測定各樣品之中央位置,設為該5點之平均值。關於L值,若膜厚度變薄則檢測器之感度變遲鈍而無法進行準確評價,故重疊總厚度達到50μm以上之最小片數而進行測定。尤其對於10μm以下之厚度之膜,採用以總厚度達到50~60μm之方式重疊膜而測定之值。 The film L value was measured using SM-7-CH manufactured by SUGA TEST INSTRUMENTS. A film of 100 mm×100 mm was divided into 5 in the film width direction, and the center position of each sample was measured and set as the average of the 5 points. Regarding the L value, if the film thickness becomes thinner, the sensitivity of the detector becomes dull and accurate evaluation cannot be performed. Therefore, the total thickness of the stack reaches the minimum number of pieces of 50 μm or more and the measurement is performed. Especially for films with a thickness of 10μm or less, the value measured by overlapping the films so that the total thickness reaches 50-60μm.

(4)耐鹼性 (4) Alkali resistance

於將5%之氫氧化鈉水溶液加熱至50℃之狀態下,使經切割成200mm×200mm之膜浸漬於其中,30分鐘後取出,測定其斷裂強度、及斷裂伸長率。將鹼浸漬前之斷裂強度、及斷裂伸長率分別設為100%,算出鹼浸漬後之該等之保持率,評價耐鹼性。將斷裂強度及斷裂伸長率之保持率兩者為80%以上之情形判斷為耐鹼性優異(○),將未達80%之情形判斷為耐鹼性較差(×)。 Under the state of heating 5% sodium hydroxide aqueous solution to 50°C, immerse the film cut into 200mm×200mm in it, take it out after 30 minutes, and measure its breaking strength and breaking elongation. The breaking strength and breaking elongation before alkali immersion were each set to 100%, and the retention rates after alkali immersion were calculated to evaluate alkali resistance. The case where both the retention of breaking strength and breaking elongation were 80% or more was judged to be excellent in alkali resistance (○), and the case where it was less than 80% was judged to be poor in alkali resistance (×).

(5)製膜性(製膜穩定性) (5) Film forming properties (film forming stability)

將於膜長度5000m之連續製膜中未產生由皺褶或破裂所引起之膜破損之情形視為○,將產生之情形視為×。 The case where there is no film damage caused by wrinkles or cracks during continuous film production with a film length of 5000m is regarded as ○, and the case where occurrence is regarded as ×.

(合成例1) (Synthesis example 1)

以莫耳比為65/35/82/18之比例準備苯均四酸二酐(分子量218.12)/3,3',4,4'-聯苯四羧酸二酐(分子量294.22)/4,4'-二胺基二苯基醚(分子量200.24)/對苯二胺(分子量108.14),製成DMAC(N,N-二甲基乙醯胺)中20重量%溶液而進行聚合,獲得於25℃下為3800泊之聚醯胺酸溶液。於該聚醯胺酸溶液中,混合相對於聚醯胺酸單元而為2.0mol 之經乾燥之N,N-二甲基乙醯胺、相對於聚醯胺酸單元而4.0mol之乙酸酐、相對於聚醯胺酸單元而為4.0mol之β-甲基吡啶,製備聚醯胺酸溶液。 Prepare pyromellitic dianhydride (molecular weight 218.12)/3,3',4,4'-biphenyltetracarboxylic dianhydride (molecular weight 294.22)/4, in a molar ratio of 65/35/82/18 4'-diaminodiphenyl ether (molecular weight 200.24)/p-phenylenediamine (molecular weight 108.14), prepared as a 20% by weight solution in DMAC (N,N-dimethylacetamide) and polymerized to obtain 3800 poise of polyamide acid solution at 25°C. In this polyamic acid solution, the mixing is 2.0 mol relative to the polyamic acid unit The dried N,N-dimethylacetamide, 4.0 mol of acetic anhydride relative to the polyamide acid unit, and 4.0 mol of β-picoline relative to the polyamide acid unit to prepare polyamide Amino acid solution.

(合成例2) (Synthesis example 2)

以莫耳比為65/35/75/25之比例準備苯均四酸二酐(分子量218.12)/3,3',4,4'-聯苯四羧酸二酐(分子量294.22)/4,4'-二胺基二苯基醚(分子量200.24)/對苯二胺(分子量108.14),製成DMAC(N,N-二甲基乙醯胺)中20重量%溶液而進行聚合,獲得於25℃下為3800泊之聚醯胺酸溶液。於該聚醯胺酸溶液中,混合相對於聚醯胺酸單元而為2.0mol之經乾燥之N,N-二甲基乙醯胺、相對於聚醯胺酸單元而為4.0mol之乙酸酐、相對於聚醯胺酸單元而為4.0mol之β-甲基吡啶,製備聚醯胺酸溶液。 Prepare pyromellitic dianhydride (molecular weight 218.12)/3,3',4,4'-biphenyltetracarboxylic dianhydride (molecular weight 294.22)/4 in the molar ratio of 65/35/75/25 4'-diaminodiphenyl ether (molecular weight 200.24)/p-phenylenediamine (molecular weight 108.14), prepared as a 20% by weight solution in DMAC (N,N-dimethylacetamide) and polymerized to obtain 3800 poise of polyamide acid solution at 25°C. In the polyamide acid solution, 2.0 mol of dried N,N-dimethylacetamide relative to the polyamide acid unit and 4.0 mol of acetic anhydride relative to the polyamide acid unit were mixed , 4.0 mol of β-picoline relative to the polyamide unit to prepare a polyamide acid solution.

(合成例3) (Synthesis example 3)

以莫耳比為65/35/67/33之比例準備苯均四酸二酐(分子量218.12)/3,3',4,4'-聯苯四羧酸二酐(分子量294.22)/4,4'-二胺基二苯基醚(分子量200.24)/對苯二胺(分子量108.14),製成DMAC(N,N-二甲基乙醯胺)中20重量%溶液而進行聚合,獲得於25℃下為3800泊之聚醯胺酸溶液。於該聚醯胺酸溶液中,混合相對於聚醯胺酸單元而為2.0mol之經乾燥之N,N-二甲基乙醯胺、相對於聚醯胺酸單元而為4.0mol之乙酸酐、相對於聚醯胺酸單元而為4.0mol之β-甲基吡啶,製備聚醯胺酸溶液。 Prepare pyromellitic dianhydride (molecular weight 218.12)/3,3',4,4'-biphenyltetracarboxylic dianhydride (molecular weight 294.22)/4 in the molar ratio of 65/35/67/33. 4'-diaminodiphenyl ether (molecular weight 200.24)/p-phenylenediamine (molecular weight 108.14), prepared as a 20% by weight solution in DMAC (N,N-dimethylacetamide) and polymerized to obtain 3800 poise of polyamide acid solution at 25°C. In the polyamide acid solution, 2.0 mol of dried N,N-dimethylacetamide relative to the polyamide acid unit and 4.0 mol of acetic anhydride relative to the polyamide acid unit were mixed , 4.0 mol of β-picoline relative to the polyamide unit to prepare a polyamide acid solution.

(合成例4) (Synthesis example 4)

以莫耳比為45/55/67/33之比例準備苯均四酸二酐(分子量218.12)/3,3',4,4'-聯苯四羧酸二酐(分子量294.22)/4,4'-二胺基二苯基醚(分子量200.24)/對苯二胺(分子量108.14),製成DMAC(N,N-二甲基乙醯胺)中20重量%溶液而進行聚合,獲得於25℃下為3800泊之聚醯胺 酸溶液。於該聚醯胺酸溶液中,混合相對於聚醯胺酸單元而為2.0mol之經乾燥之N,N-二甲基乙醯胺、相對於聚醯胺酸單元而為4.0mol之乙酸酐、相對於聚醯胺酸單元而為4.0mol之β-甲基吡啶,製備聚醯胺酸溶液。 Prepare pyromellitic dianhydride (molecular weight 218.12)/3,3',4,4'-biphenyltetracarboxylic dianhydride (molecular weight 294.22)/4 in a molar ratio of 45/55/67/33. 4'-diaminodiphenyl ether (molecular weight 200.24)/p-phenylenediamine (molecular weight 108.14), prepared as a 20% by weight solution in DMAC (N,N-dimethylacetamide) and polymerized to obtain 3800 poise of polyamide at 25℃ Acid solution. In the polyamide acid solution, 2.0 mol of dried N,N-dimethylacetamide relative to the polyamide acid unit and 4.0 mol of acetic anhydride relative to the polyamide acid unit were mixed , 4.0 mol of β-picoline relative to the polyamide unit to prepare a polyamide acid solution.

(實施例1) (Example 1)

將合成例1之聚醯胺酸溶液自噴嘴狹縫寬度1.3mm、長度2000mm之T型模頭中擠出,將支撐體速度/噴嘴噴出速度之比設為10.6,流延至旋轉之80℃的金屬支撐體上,獲得具有自我支撐性之凝膠膜。將該凝膠膜自支撐體上連續剝下,於70℃之室內一面於膜長邊方向上延伸至1.22倍一面用輥進行搬送。一面以輥按壓凝膠膜之兩端,一面連續紮刺鏈條上之針板而固定凝膠膜,向針板上吹附250℃之空氣5~10秒鐘,藉此先將凝膠膜乾燥固定。將於針板上以針固定兩端之凝膠膜於寬度方向上延伸至1.40倍後,於拉幅機內吹附250℃之空氣約20秒鐘,藉此加以乾燥,繼而使用電加熱器實施約30秒鐘之熱處理以使膜表面溫度達到450℃後,一面使其鬆弛一面冷卻至室溫。然後,將膜端部自針上取下,切割膜之端部之邊緣,藉此獲得寬度2100mm、厚度7.6μm之聚醯亞胺膜。製膜中膜未產生皺褶或破裂,可穩定地以長度5000m以上製膜。所獲得之膜之L值(以7片重疊測定)為35.0。又,評價耐鹼性,結果斷裂強度保持率為96%、斷裂伸長率保持率為97%之良好之值。 The polyamide acid solution of Synthesis Example 1 was extruded from a T-die with a nozzle slit width of 1.3 mm and a length of 2000 mm. The ratio of the support speed/the nozzle ejection speed was set to 10.6, and the solution was cast to a rotating temperature of 80°C. On the metal support, a self-supporting gel film is obtained. The gel film was continuously peeled off from the support, and was transported with a roller on one side extending 1.22 times in the longitudinal direction of the film in a room at 70°C. While pressing the two ends of the gel film with a roller, the needle plate on the chain is continuously pierced to fix the gel film, and air of 250℃ is blown on the needle plate for 5-10 seconds to dry the gel film first fixed. After the gel film on the two ends of the needle plate fixed with needles is extended to 1.40 times in the width direction, blow 250℃ air in the tenter for about 20 seconds to dry it, and then use an electric heater After performing heat treatment for about 30 seconds to bring the film surface temperature to 450°C, it was cooled to room temperature while being relaxed. Then, the end of the film was removed from the needle, and the edge of the end of the film was cut to obtain a polyimide film with a width of 2100 mm and a thickness of 7.6 μm. There is no wrinkles or cracks in the film during film production, and the film can be stably formed with a length of 5000m or more. The L value (measured by overlapping 7 sheets) of the obtained film was 35.0. In addition, the alkali resistance was evaluated. As a result, the retention of breaking strength was 96% and the retention of elongation at break was 97%.

(實施例2) (Example 2)

將合成例1之聚醯胺酸溶液自噴嘴狹縫寬度1.3mm、長度2000mm之T型模頭中擠出,將支撐體速度/噴嘴噴出速度之比設為10.6,流延至旋轉之80℃的金屬支撐體上,獲得具有自我支撐性之凝膠膜。將該凝膠膜自支撐體上連續剝下,於70℃之室內一面於膜長邊方向上延伸至1.22倍一面用輥進行搬送。一面以輥按壓凝膠膜之兩端一面連 續紮刺鏈條上之針板而固定凝膠膜,向針板上吹送250℃之空氣5~10秒鐘,藉此先將凝膠膜端部乾燥固定。將於針板上以針固定兩端之凝膠膜於寬度方向上延伸至1.40倍後,於拉幅機內吹附250℃之空氣約20秒鐘,藉此加以乾燥,繼而使用電加熱器實施約30秒鐘之熱處理以使膜表面溫度達到475℃後,一面使其鬆弛一面冷卻至室溫。然後,將膜端部自針上取下,切割膜之端部之邊緣,藉此獲得寬度2100mm、厚度7.6μm之聚醯亞胺膜。製膜中膜未產生皺褶或破裂,可穩定地以長度5000m以上製膜。所獲得之膜之L值(以7片重疊測定)為31.3。又,評價耐鹼性,結果斷裂強度保持率為94%、斷裂伸長率保持率為101%之良好之值。 The polyamide acid solution of Synthesis Example 1 was extruded from a T-die with a nozzle slit width of 1.3 mm and a length of 2000 mm. The ratio of the support speed/the nozzle ejection speed was set to 10.6, and the solution was cast to a rotating temperature of 80°C. On the metal support, a self-supporting gel film is obtained. The gel film was continuously peeled off from the support, and was transported with a roller on one side extending 1.22 times in the longitudinal direction of the film in a room at 70°C. While pressing the two ends of the gel film with a roller, Continue to pierce the needle plate on the chain to fix the gel film, and blow 250℃ air on the needle plate for 5-10 seconds to dry and fix the end of the gel film. After the gel film on the two ends of the needle plate fixed with needles is extended to 1.40 times in the width direction, blow 250℃ air in the tenter for about 20 seconds to dry it, and then use an electric heater After performing heat treatment for about 30 seconds to bring the film surface temperature to 475°C, it was cooled to room temperature while being relaxed. Then, the end of the film was removed from the needle, and the edge of the end of the film was cut to obtain a polyimide film with a width of 2100 mm and a thickness of 7.6 μm. There is no wrinkles or cracks in the film during film production, and the film can be stably formed with a length of 5000m or more. The L value (measured by overlapping 7 sheets) of the obtained film was 31.3. In addition, the alkali resistance was evaluated. As a result, the retention of breaking strength was 94% and the retention of elongation at break was 101%.

(實施例3) (Example 3)

將合成例2之聚醯胺酸溶液自噴嘴狹縫寬度1.3mm、長度2000mm之T型模頭擠出,將支撐體速度/噴嘴噴出速度之比設為8.6,流延至旋轉之80℃的金屬支撐體上,獲得具有自我支撐性之凝膠膜。將該凝膠膜自支撐體上連續剝下,於70℃之室內一面於膜長邊方向上延伸至1.31倍一面用輥進行搬送。一面以輥按壓凝膠膜之兩端一面連續紮刺鏈條上之針板而固定凝膠膜,向針板上吹附250℃之空氣5~10秒鐘,藉此先將固定凝膠膜端部乾燥。將於針板上以針固定兩端之凝膠膜於寬度方向上延伸至1.62倍後,於拉幅機內吹附250℃之空氣約25秒鐘,藉此加以乾燥,繼而使用電加熱器實施約35秒鐘之熱處理以使膜表面溫度達到435℃後,一面使其鬆弛一面冷卻至室溫。然後,將膜端部自針上取下,切割膜之端部之邊緣,藉此獲得寬度2100mm、厚度7.4μm之聚醯亞胺膜。製膜中膜未產生皺褶或破裂,可穩定地以長度5000m以上製膜。所獲得之膜之L值(以7片重疊測定)為38.3。又,評價耐鹼性,結果斷裂強度保持率為109%、斷裂伸長率保持率為116%之良好之值。 The polyamide acid solution of Synthesis Example 2 was extruded from a T-die with a nozzle slit width of 1.3 mm and a length of 2000 mm, and the ratio of support speed/nozzle ejection speed was set to 8.6, and cast to a rotating metal at 80°C On the support, a self-supporting gel film is obtained. The gel film was continuously peeled off from the support, and it was transported with a roller while extending 1.31 times in the longitudinal direction of the film in a room at 70°C. While pressing the two ends of the gel film with a roller, the needle plate on the chain is continuously pierced to fix the gel film, and air of 250℃ is blown on the needle plate for 5-10 seconds to fix the end of the gel film. Department is dry. After the gel film on the two ends of the needle plate fixed with needles is stretched to 1.62 times in the width direction, blow 250℃ air in the tenter for about 25 seconds to dry it, and then use an electric heater After performing heat treatment for about 35 seconds to bring the film surface temperature to 435°C, it was cooled to room temperature while being relaxed. Then, the end of the film was removed from the needle, and the edge of the end of the film was cut to obtain a polyimide film with a width of 2100 mm and a thickness of 7.4 μm. There is no wrinkles or cracks in the film during film production, and the film can be stably formed with a length of 5000m or more. The L value (measured by overlapping 7 sheets) of the obtained film was 38.3. In addition, the alkali resistance was evaluated. As a result, the breaking strength retention rate was 109%, and the breaking elongation retention rate was 116%.

(實施例4) (Example 4)

將合成例3之聚醯胺酸溶液自噴嘴狹縫寬度1.3mm、長度2000mm之T型模頭中擠出,將支撐體速度/噴嘴噴出速度之比設為9.0,流延至旋轉之80℃的金屬支撐體上,獲得具有自我支撐性之凝膠膜。將該凝膠膜自支撐體上連續剝下,於70℃之室內一面於膜長邊方向上延伸至1.28倍一面用輥進行搬送。一面以輥按壓凝膠膜之兩端一面連續紮刺鏈條上之針板而固定凝膠膜,向針板上吹附250℃之空氣5~10秒鐘,藉此先將凝膠膜端部乾燥固定。將於針板上以針固定兩端之凝膠膜於寬度方向上延伸至1.59倍後,於拉幅機內吹附250℃之空氣25秒鐘,藉此加以乾燥,繼而使用電加熱器實施約35秒鐘之熱處理以使膜表面溫度達到435℃後,一面使其鬆弛一面冷卻至室溫。然後,將膜端部自針上取下,切割膜之端部之邊緣,藉此獲得寬度2100mm、厚度7.5μm之聚醯亞胺膜。製膜中膜未產生皺褶或破裂,可穩定地以長度5000m以上製膜。所獲得之膜之L值(以7片重疊測定)為38.5。又,評價耐鹼性,結果斷裂強度保持率為90%、斷裂伸長率保持率為100%之良好之值。 The polyamide acid solution of Synthesis Example 3 was extruded from a T-die with a nozzle slit width of 1.3 mm and a length of 2000 mm, and the ratio of support speed/nozzle ejection speed was set to 9.0, and it was cast to a rotating temperature of 80°C. On the metal support, a self-supporting gel film is obtained. The gel film was continuously peeled off from the support, and was transported with a roller while extending 1.28 times in the longitudinal direction of the film in a room at 70°C. While pressing the two ends of the gel film with a roller, the needle plate on the chain is continuously pierced to fix the gel film, and air of 250℃ is blown on the needle plate for 5-10 seconds, thereby firstly removing the ends of the gel film Dry and fix. After the gel film on the two ends of the needle board fixed with the needles is extended to 1.59 times in the width direction, the air of 250℃ is blown in the tenter for 25 seconds to dry it, and then the electric heater is used for implementation. After heat treatment for about 35 seconds to bring the surface temperature of the film to 435°C, it was cooled to room temperature while being relaxed. Then, the end of the film was removed from the needle, and the edge of the end of the film was cut to obtain a polyimide film with a width of 2100 mm and a thickness of 7.5 μm. There is no wrinkles or cracks in the film during film production, and the film can be stably formed with a length of 5000m or more. The L value (measured by overlapping 7 sheets) of the obtained film was 38.5. In addition, the alkali resistance was evaluated. As a result, the breaking strength retention rate was 90%, and the breaking elongation retention rate was 100%, which were good values.

(實施例5) (Example 5)

將合成例3之聚醯胺酸溶液自噴嘴狹縫寬度1.3mm、長度2000mm之T型模頭中擠出,將支撐體速度/噴嘴噴出速度之比設為9.0,流延至旋轉之80℃的金屬支撐體上,獲得具有自我支撐性之凝膠膜。將該凝膠膜自支撐體上連續剝下,於70℃之室內一面於膜長邊方向上延伸至1.28倍一面用輥進行搬送。一面以輥按壓凝膠膜之兩端一面連續紮刺鏈條上之針板而固定凝膠膜,向針板上吹附250℃之空氣5~10秒鐘,藉此先將凝膠膜端部乾燥固定。將於針板上以針固定兩端之凝膠膜於寬度方向上延伸至1.59倍後,於拉幅機內吹附250℃之空氣約20秒鐘,藉此加以乾燥,繼而使用電加熱器實施約30秒鐘之熱處理以使 膜表面溫度達到465℃後,一面使其鬆弛一面冷卻至室溫。然後,將膜端部自針上取下,切割膜之端部之邊緣,藉此獲得寬度2100mm、厚度7.5μm之聚醯亞胺膜。製膜中膜未產生皺褶或破裂,可穩定地以長度5000m以上製膜。所獲得之膜之L值(以7片重疊測定)為32.5。又,評價耐鹼性,結果斷裂強度保持率為94%、斷裂伸長率保持率為100%之良好之值。 The polyamide acid solution of Synthesis Example 3 was extruded from a T-die with a nozzle slit width of 1.3 mm and a length of 2000 mm, and the ratio of support speed/nozzle ejection speed was set to 9.0, and it was cast to a rotating temperature of 80°C. On the metal support, a self-supporting gel film is obtained. The gel film was continuously peeled off from the support, and was transported with a roller while extending 1.28 times in the longitudinal direction of the film in a room at 70°C. While pressing the two ends of the gel film with a roller, the needle plate on the chain is continuously pierced to fix the gel film, and air of 250℃ is blown on the needle plate for 5-10 seconds, thereby firstly removing the ends of the gel film Dry and fix. After the gel film on the two ends of the needle plate fixed with needles is extended to 1.59 times in the width direction, blow 250℃ air in the tenter for about 20 seconds to dry it, and then use an electric heater Perform heat treatment for about 30 seconds to make After the film surface temperature reached 465°C, it was allowed to relax while cooling to room temperature. Then, the end of the film was removed from the needle, and the edge of the end of the film was cut to obtain a polyimide film with a width of 2100 mm and a thickness of 7.5 μm. There is no wrinkles or cracks in the film during film production, and the film can be stably formed with a length of 5000m or more. The L value of the obtained film (measured by overlapping 7 sheets) was 32.5. In addition, the alkali resistance was evaluated. As a result, the retention rate of breaking strength was 94%, and the retention rate of breaking elongation was 100%.

(實施例6) (Example 6)

將合成例4之聚醯胺酸溶液自噴嘴狹縫寬度1.3mm、長度2000mm之T型模頭中擠出,將支撐體速度/噴嘴噴出速度之比設為9.1,流延至旋轉之80℃的金屬支撐體上,獲得具有自我支撐性之凝膠膜。將該凝膠膜自支撐體上連續剝下,於70℃之室內一面於膜長邊方向上延伸至1.28倍一面用輥進行搬送。一面以輥按壓凝膠膜之兩端一面連續紮刺鏈條上針板而固定凝膠膜,向針板上吹附250℃之空氣5~10秒鐘,藉此先將凝膠膜端部乾燥固定。將於針板上以針固定兩端之凝膠膜於寬度方向上延伸至1.55倍後,於拉幅機內吹附250℃之空氣約25秒鐘,藉此加以乾燥,繼而使用電加熱器實施約30秒鐘之熱處理以使膜表面溫度達到415℃後,一面使其鬆弛一面冷卻至室溫。然後,將膜端部自針上取下,切割膜之端部之邊緣,藉此獲得寬度2100mm、厚度7.5μm之聚醯亞胺膜。製膜中膜未產生皺褶或破裂,可穩定地以長度5000m以上製膜。所獲得之膜之L值(以7片重疊測定)為41.5。又,評價耐鹼性,結果斷裂強度保持率為92%、斷裂伸長率保持率為97%之良好之值。 The polyamide acid solution of Synthesis Example 4 was extruded from a T-die with a nozzle slit width of 1.3 mm and a length of 2000 mm, and the ratio of support speed/nozzle ejection speed was set to 9.1, and it was cast to a rotating temperature of 80°C. On the metal support, a self-supporting gel film is obtained. The gel film was continuously peeled off from the support, and was transported with a roller while extending 1.28 times in the longitudinal direction of the film in a room at 70°C. While pressing the two ends of the gel film with a roller, the needle plate of the chain is continuously pierced to fix the gel film, and air of 250℃ is blown on the needle plate for 5-10 seconds to dry the ends of the gel film first fixed. After the gel film on the two ends of the needle plate fixed with needles is stretched to 1.55 times in the width direction, blow 250℃ air in the tenter for about 25 seconds to dry it, and then use an electric heater After performing heat treatment for about 30 seconds to bring the film surface temperature to 415°C, it was cooled to room temperature while being relaxed. Then, the end of the film was removed from the needle, and the edge of the end of the film was cut to obtain a polyimide film with a width of 2100 mm and a thickness of 7.5 μm. There is no wrinkles or cracks in the film during film production, and the film can be stably formed with a length of 5000m or more. The L value (measured by overlapping 7 sheets) of the obtained film was 41.5. In addition, when the alkali resistance was evaluated, the breaking strength retention rate was 92%, and the breaking elongation retention rate was 97%.

(實施例7) (Example 7)

將合成例4之聚醯胺酸溶液自噴嘴狹縫寬度1.3mm、長度2000mm之T型模頭中擠出,將支撐體速度/噴嘴噴出速度之比設為9.1,流延至旋轉之80℃的金屬支撐體上,獲得具有自我支撐性之凝膠膜。將 該凝膠膜自支撐體上連續剝下,於70℃之室內一面於膜長邊方向上延伸至1.28倍一面用輥進行搬送。一面以輥按壓凝膠膜之兩端一面連續紮刺鏈條上之針板而固定凝膠膜,向針板上吹附250℃之空氣5~10秒鐘,藉此先將凝膠膜端部乾燥固定。將於針板上以針固定兩端之凝膠膜於寬度方向上延伸至1.55倍後,於拉幅機內吹附250℃之空氣約25秒鐘,藉此加以乾燥,繼而使用電加熱器實施約35秒鐘之熱處理以使膜表面溫度達到445℃後,一面使其鬆弛一面冷卻至室溫。然後,將膜端部自針上取下,切割膜之端部之邊緣,藉此獲得寬度2100mm、厚度7.5μm之聚醯亞胺膜。製膜中膜未產生皺褶或破裂,可穩定地以長度5000m以上製膜。所獲得之膜之L值(以7片重疊測定)為36.7。又,評價耐鹼性,結果斷裂強度保持率為91%、斷裂伸長率保持率為88%之良好之值。 The polyamide acid solution of Synthesis Example 4 was extruded from a T-die with a nozzle slit width of 1.3 mm and a length of 2000 mm, and the ratio of support speed/nozzle ejection speed was set to 9.1, and it was cast to a rotating temperature of 80°C. On the metal support, a self-supporting gel film is obtained. will The gel film was continuously peeled off from the support, and was transported with a roller on one side extended to 1.28 times in the longitudinal direction of the film in a room at 70°C. While pressing the two ends of the gel film with a roller, the needle plate on the chain is continuously pierced to fix the gel film, and air of 250℃ is blown on the needle plate for 5-10 seconds, thereby firstly removing the ends of the gel film Dry and fix. After the gel film on the two ends of the needle plate fixed with needles is stretched to 1.55 times in the width direction, blow 250℃ air in the tenter for about 25 seconds to dry it, and then use an electric heater After performing heat treatment for about 35 seconds to bring the film surface temperature to 445°C, it was cooled to room temperature while being relaxed. Then, the end of the film was removed from the needle, and the edge of the end of the film was cut to obtain a polyimide film with a width of 2100 mm and a thickness of 7.5 μm. There is no wrinkles or cracks in the film during film production, and the film can be stably formed with a length of 5000m or more. The L value (measured by overlapping 7 sheets) of the obtained film was 36.7. In addition, the alkali resistance was evaluated. As a result, the retention of breaking strength was 91% and the retention of elongation at break was 88%.

(實施例8) (Example 8)

將合成例3之聚醯胺酸溶液自噴嘴狹縫寬度1.3mm、長度2000mm之T型模頭中擠出,將支撐體速度/噴嘴噴出速度之比設為14.2,流延至旋轉之80℃的金屬支撐體上,獲得具有自我支撐性之凝膠膜。將該凝膠膜自支撐體上連續剝下,於70℃之室內一面於膜長邊方向延伸至1.28倍一面用輥進行搬送。一面以輥按壓凝膠膜之兩端一面連續紮刺鏈條上之針板而固定凝膠膜,向針板上吹附240℃之空氣5~10秒鐘,藉此先將凝膠膜端部乾燥固定。將於針板上以針固定兩端之凝膠膜於寬度方向上延伸至1.62倍後,於拉幅機內吹附240℃之空氣約20秒鐘,藉此加以乾燥,繼而使用電加熱器實施約30秒鐘之熱處理以使膜表面溫度達到435℃後,一面使其鬆弛一面冷卻至室溫。然後,將膜端部自針上取下,切割膜之端部之邊緣,藉此獲得寬度2100mm、厚度5.0μm之聚醯亞胺膜。製膜中膜未產生皺褶或破裂,可穩定地以長度5000m以上製膜。所獲得之膜之L值(以10片重疊測定)為36.5。 又,評價耐鹼性,結果斷裂強度保持率為90%、斷裂伸長率保持率為92%之良好之值。 The polyamide acid solution of Synthesis Example 3 was extruded from a T-die with a nozzle slit width of 1.3 mm and a length of 2000 mm, and the ratio of support speed/nozzle ejection speed was set to 14.2, and it was cast to a rotating temperature of 80°C. On the metal support, a self-supporting gel film is obtained. The gel film was continuously peeled off from the support, and was transported with a roller while extending 1.28 times in the longitudinal direction of the film in a room at 70°C. While pressing the two ends of the gel film with a roller, the needle plate on the chain is continuously pierced to fix the gel film, and air of 240℃ is blown on the needle plate for 5-10 seconds, thereby firstly removing the ends of the gel film Dry and fix. After the gel film on the two ends of the needle plate fixed with needles is extended to 1.62 times in the width direction, blow 240℃ air in the tenter for about 20 seconds to dry it, and then use an electric heater After performing a heat treatment for about 30 seconds to bring the film surface temperature to 435°C, it was cooled to room temperature while being relaxed. Then, the end of the film was removed from the needle, and the edge of the end of the film was cut to obtain a polyimide film with a width of 2100 mm and a thickness of 5.0 μm. There is no wrinkles or cracks in the film during film production, and the film can be stably formed with a length of 5000m or more. The L value of the obtained film (measured by overlapping 10 sheets) was 36.5. In addition, the alkali resistance was evaluated. As a result, the breaking strength retention rate was 90%, and the breaking elongation retention rate was 92%, which were good values.

(實施例9) (Example 9)

將合成例1之聚醯胺酸溶液自噴嘴狹縫寬度1.3mm、長度2000mm之T型模頭中擠出,將支撐體速度/噴嘴噴出速度之比設為6.0,流延至旋轉之80℃的金屬支撐體上,獲得具有自我支撐性之凝膠膜。將該凝膠膜自支撐體上連續剝下,於70℃之室內一面於膜長邊方向上延伸至1.22倍一面用輥進行搬送。一面以輥按壓凝膠膜之兩端一面連續紮刺鏈條上之針板而固定凝膠膜,向針板上吹附250℃之空氣5~10秒鐘,藉此先將凝膠膜端部乾燥固定。將於針板上以針固定兩端之凝膠膜於寬度方向上延伸至1.45倍後,於拉幅機內吹附250℃之空氣約40秒鐘,藉此加以乾燥,繼而使用電加熱器實施約60秒鐘之熱處理以使膜表面溫度達到400℃後,一面使其鬆弛一面冷卻至室溫。然後,將膜端部自針上取下,切割膜之端部之邊緣,藉此獲得寬度2100mm、厚度10.0μm之聚醯亞胺膜。製膜中膜未產生皺褶或破裂,可穩定地以長度5000m以上製膜。所獲得之膜之L值(以5片重疊測定)為42.5。又,評價耐鹼性,結果斷裂強度保持率為98%、斷裂伸長率保持率為98%之良好之值。 The polyamide acid solution of Synthesis Example 1 was extruded from a T-die with a nozzle slit width of 1.3 mm and a length of 2000 mm, and the ratio of support speed/nozzle ejection speed was set to 6.0, and it was cast to a rotating temperature of 80°C. On the metal support, a self-supporting gel film is obtained. The gel film was continuously peeled off from the support, and was transported with a roller on one side extending 1.22 times in the longitudinal direction of the film in a room at 70°C. While pressing the two ends of the gel film with a roller, the needle plate on the chain is continuously pierced to fix the gel film, and air of 250℃ is blown on the needle plate for 5-10 seconds, thereby firstly removing the ends of the gel film Dry and fix. After the gel film on the two ends of the needle plate fixed with needles is extended to 1.45 times in the width direction, blow 250℃ air in the tenter for about 40 seconds to dry it, and then use an electric heater After performing heat treatment for about 60 seconds to bring the film surface temperature to 400°C, it was cooled to room temperature while being relaxed. Then, the end of the film was removed from the needle, and the edge of the end of the film was cut to obtain a polyimide film with a width of 2100 mm and a thickness of 10.0 μm. There is no wrinkles or cracks in the film during film production, and the film can be stably formed with a length of 5000m or more. The L value (measured by overlapping 5 sheets) of the obtained film was 42.5. In addition, the alkali resistance was evaluated. As a result, the retention of breaking strength was 98% and the retention of elongation at break was 98%, which were good values.

(參考例1) (Reference example 1)

將合成例3之聚醯胺酸溶液自噴嘴狹縫寬度1.3mm、長度2000mm之T型模頭中擠出,將支撐體速度/噴嘴噴出速度之比設為8.3,流延至旋轉之80℃的金屬支撐體上,獲得具有自我支撐性之凝膠膜。將該凝膠膜自支撐體上連續剝下,於70℃之室內一面於膜長邊方向上延伸至1.28倍一面用輥進行搬送。一面以輥按壓凝膠膜之兩端一面連續紮刺鏈條上之針板而固定凝膠膜,向針板上吹附250℃之空氣5~10秒鐘,藉此先將凝膠膜端部乾燥固定。將於針板上以針固定兩端之凝膠 膜於寬度方向上延伸至1.59倍後,於拉幅機內吹附250℃之空氣約35秒鐘,藉此加以乾燥,繼而使用電加熱器實施約35秒鐘之熱處理以使膜表面溫度達到500℃後,一面使其鬆弛一面冷卻至室溫。然後,將膜端部自針上取下,切割膜之端部之邊緣,藉此獲得寬度2100mm、厚度7.5μm之聚醯亞胺膜。然而,自達到上述條件後製膜600m後將膜端部自針上取下時膜破裂,產生了膜破損。膜即將破損之前之膜之L值(以7片重疊測定)為27.1。評價耐鹼性,結果斷裂強度保持率為96%、斷裂伸長率保持率為101%之良好之值。 The polyamide acid solution of Synthesis Example 3 was extruded from a T-die with a nozzle slit width of 1.3 mm and a length of 2000 mm, and the ratio of support speed/nozzle ejection speed was set to 8.3, and it was cast to a rotating temperature of 80°C. On the metal support, a self-supporting gel film is obtained. The gel film was continuously peeled off from the support, and was transported with a roller while extending 1.28 times in the longitudinal direction of the film in a room at 70°C. While pressing the two ends of the gel film with a roller, the needle plate on the chain is continuously pierced to fix the gel film, and air of 250℃ is blown on the needle plate for 5-10 seconds, thereby firstly removing the ends of the gel film Dry and fix. Fix the gel at both ends with needles on the needle board After the film is stretched to 1.59 times in the width direction, air at 250°C is blown in the tenter for about 35 seconds to dry it, and then an electric heater is used to perform heat treatment for about 35 seconds to make the film surface temperature reach After 500°C, cool to room temperature while relaxing it. Then, the end of the film was removed from the needle, and the edge of the end of the film was cut to obtain a polyimide film with a width of 2100 mm and a thickness of 7.5 μm. However, after the above conditions were met, the film was formed for 600 m and the end of the film was removed from the needle when the film was broken, resulting in film breakage. The L value of the film immediately before the film breakage (measured by overlapping 7 sheets) was 27.1. The alkali resistance was evaluated. As a result, the retention rate of breaking strength was 96%, and the retention rate of breaking elongation was 101%.

(參考例2) (Reference example 2)

將合成例1之聚醯胺酸溶液自噴嘴狹縫寬度1.3mm、長度2000mm之T型模頭中擠出,將支撐體速度/噴嘴噴出速度之比設為10.6,流延至旋轉之80℃的金屬支撐體上,獲得具有自我支撐性之凝膠膜。將該凝膠膜自支撐體上連續剝離,於70℃之室內一面於膜長邊方向上延伸至1.22倍一面用輥進行搬送。一面以輥按壓凝膠膜之兩端一面連續紮刺鏈條上之針板而固定凝膠膜,向針板上吹附250℃之空氣5~10秒鐘,藉此先將凝膠膜端部乾燥固定。將於針板上以針固定兩端之凝膠膜於寬度方向上延伸至1.40倍後,於拉幅機內吹附250℃之空氣約20秒鐘,藉此加以乾燥,繼而使用電加熱器實施約30秒鐘之熱處理以使膜表面溫度達到400℃後,一面使其鬆弛一面冷卻至室溫。然後,將膜端部自針上取下,切割膜之端部之邊緣,藉此獲得寬度2100mm、厚度7.5μm之聚醯亞胺膜。製膜中膜未產生皺褶或破裂,可穩定地以長度5000m以上製膜。所獲得之膜之L值(以7片重疊測定)為45.2。又,評價耐鹼性,結果確認到斷裂強度保持率劣化至69%,斷裂伸長率保持率劣化至34%。 The polyamide acid solution of Synthesis Example 1 was extruded from a T-die with a nozzle slit width of 1.3 mm and a length of 2000 mm. The ratio of the support speed/the nozzle ejection speed was set to 10.6, and the solution was cast to a rotating temperature of 80°C. On the metal support, a self-supporting gel film is obtained. The gel film was continuously peeled from the support, and was transported with a roller while extending 1.22 times the length of the film in the longitudinal direction of the film in a room at 70°C. While pressing the two ends of the gel film with a roller, the needle plate on the chain is continuously pierced to fix the gel film, and air of 250℃ is blown on the needle plate for 5-10 seconds, thereby firstly removing the ends of the gel film Dry and fix. After the gel film on the two ends of the needle plate fixed with needles is extended to 1.40 times in the width direction, blow 250℃ air in the tenter for about 20 seconds to dry it, and then use an electric heater After performing a heat treatment for about 30 seconds to bring the film surface temperature to 400°C, it was cooled to room temperature while being relaxed. Then, the end of the film was removed from the needle, and the edge of the end of the film was cut to obtain a polyimide film with a width of 2100 mm and a thickness of 7.5 μm. There is no wrinkles or cracks in the film during film production, and the film can be stably formed with a length of 5000m or more. The L value (measured by overlapping 7 sheets) of the obtained film was 45.2. In addition, the alkali resistance was evaluated, and as a result, it was confirmed that the breaking strength retention rate deteriorated to 69%, and the breaking elongation rate retention rate deteriorated to 34%.

【表1】

Figure 105107078-A0202-12-0025-2
【Table 1】
Figure 105107078-A0202-12-0025-2

如由實施例1~9之結果所表明,L值為28~45之本發明之聚醯亞胺膜即便厚度薄至5.0~10.0μm,亦為斷裂強度或斷裂伸長率不易因浸漬於鹼性溶液中而降低、且耐鹼性優異者。 As shown by the results of Examples 1-9, the polyimide film of the present invention with an L value of 28 to 45, even if the thickness is as thin as 5.0 to 10.0 μm, is that the breaking strength or breaking elongation is not easy to be immersed in alkaline It is reduced in the solution and excellent in alkali resistance.

進而,L值為28~45之本發明之聚醯亞胺膜即便厚度薄至5.0~10.0μm,亦為製膜性亦優異者。 Furthermore, the polyimide film of the present invention having an L value of 28 to 45 has excellent film formability even if the thickness is as thin as 5.0 to 10.0 μm.

又,實施例1~9之本發明之聚醯亞胺膜即便厚度薄至5.0~10.0μm,亦為具有充分之斷裂強度及斷裂伸長率者。 In addition, the polyimide film of the present invention of Examples 1 to 9 has sufficient breaking strength and breaking elongation even if the thickness is as thin as 5.0 to 10.0 μm.

又,由實施例1~9之結果得知,於將聚醯亞胺之重複單元之分子量設為100%時,藉由將聚醯亞胺中之醯亞胺基之分子量設為40%以下,而成為即便厚度薄至5.0~10.0μm亦耐鹼性優異之聚醯亞胺膜。 In addition, from the results of Examples 1-9, when the molecular weight of the repeating unit of the polyimine is set to 100%, the molecular weight of the imine group in the polyimine is set to 40% or less , And become a polyimide film with excellent alkali resistance even as thin as 5.0~10.0μm.

另一方面,L值未達28之參考例1之聚醯亞胺膜為脆弱易破裂、製膜性較差者。 On the other hand, the polyimide film of Reference Example 1 in which the L value was less than 28 was fragile and easy to break, with poor film forming properties.

又,L值大於45之參考例2之聚醯亞胺膜係耐鹼性較差,斷裂強 度及斷裂伸長率因浸漬於鹼性溶液中而降低。 In addition, the polyimide film of Reference Example 2 with an L value greater than 45 has poor alkali resistance and strong fracture The degree and elongation at break are reduced by immersion in an alkaline solution.

如上所述般得知,藉由L值為28~45,厚度為1.0~10.0μm之薄膜聚醯亞胺膜成為可兼具耐鹼性與製膜性者。 As described above, the thin film polyimide film with an L value of 28 to 45 and a thickness of 1.0 to 10.0 μm can be both alkali resistance and film forming properties.

[產業上之可利用性] [Industrial availability]

本發明之聚醯亞胺膜儘管為厚度1.0~10.0μm之極薄膜,亦耐鹼性優異,且於膜之製造步驟中不易發生破損等,製膜穩定性良好,故可較佳地用作要求薄度之FPC之基礎膜等。 Although the polyimide film of the present invention is an extremely thin film with a thickness of 1.0~10.0μm, it is also excellent in alkali resistance, and it is not easy to be damaged during the film production step, and has good film stability, so it can be preferably used as The basic film of FPC that requires thinness.

Claims (7)

一種聚醯亞胺膜,其厚度為1.0~10.0μm,其特徵在於:於將聚醯亞胺之重複單元之分子量設為100%時,其醯亞胺基之分子量為40%以下,且聚醯亞胺膜之L值為28~42.5。 A polyimide film with a thickness of 1.0~10.0μm, characterized in that when the molecular weight of the repeating unit of the polyimide is set to 100%, the molecular weight of the polyimide group is 40% or less, and the polyimide The L value of the imine film is 28~42.5. 如請求項1之聚醯亞胺膜,其中聚醯亞胺膜係藉由膜之機械搬送方向(MD)與寬度方向(TD)之雙軸延伸處理而延伸,且膜之總延伸倍率(MD之延伸倍率×TD之延伸倍率)為1.60以上。 Such as the polyimide film of claim 1, wherein the polyimide film is stretched by biaxial stretching in the mechanical conveying direction (MD) and the width direction (TD) of the film, and the total stretching ratio (MD The extension ratio × TD extension ratio) is 1.60 or more. 如請求項1之聚醯亞胺膜,其係由芳香族二胺成分為選自由對苯二胺、4,4'-二胺基二苯基醚及3,4'-二胺基二苯基醚所組成之群中之1種以上,芳香族酸酐成分為苯均四酸二酐及/或3,3',4,4'-聯苯四羧酸二酐之聚醯胺酸而製造。 Such as the polyimide film of claim 1, which is composed of aromatic diamine components selected from p-phenylenediamine, 4,4'-diaminodiphenyl ether and 3,4'-diaminodiphenyl One or more of the group consisting of base ethers, the aromatic anhydride component is pyromellitic dianhydride and/or 3,3',4,4'-biphenyltetracarboxylic dianhydride polyamide acid . 一種聚醯亞胺膜之製造方法,其係如請求項1至3中任一項之聚醯亞胺膜之製造方法,其將可形成聚醯亞胺膜之凝膠膜進行延伸而獲得之膜於350~500℃下進行5~300秒鐘之加熱處理,上述聚醯亞胺膜係將聚醯亞胺之重複單元之分子量設為100%時,其醯亞胺基之分子量為40%以下者。 A method for manufacturing a polyimide film, which is the method for manufacturing a polyimide film according to any one of claims 1 to 3, which is obtained by extending a gel film that can form a polyimide film The film is heated at 350-500°C for 5 to 300 seconds. When the molecular weight of the repeating unit of the polyimine film is set to 100%, the molecular weight of the imine group is 40%. The following. 一種聚醯亞胺膜,其特徵在於:包含如請求項1至3中任一項之聚醯亞胺膜(A)、及積層於聚醯亞胺膜(A)之單面或者兩面上之聚醯亞胺膜(B)。 A polyimide film, characterized in that it comprises a polyimide film (A) as in any one of claims 1 to 3, and a polyimide film (A) laminated on one or both sides of the polyimide film (A) Polyimide film (B). 如請求項1至3中任一項之聚醯亞胺膜,其中聚醯亞胺膜之形態為寬度500~3000mm、長度1000m以上之聚醯亞胺膜捲。 Such as the polyimide film of any one of claims 1 to 3, wherein the form of the polyimide film is a polyimide film roll with a width of 500-3000mm and a length of 1000m or more. 如請求項1至3中任一項之聚醯亞胺膜,其係用於柔性印刷電路板。 Such as the polyimide film of any one of claims 1 to 3, which is used for flexible printed circuit boards.
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