TWI243186B - Polyimide film, manufacturing method of same, and usage of same - Google Patents

Polyimide film, manufacturing method of same, and usage of same Download PDF

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Publication number
TWI243186B
TWI243186B TW092125231A TW92125231A TWI243186B TW I243186 B TWI243186 B TW I243186B TW 092125231 A TW092125231 A TW 092125231A TW 92125231 A TW92125231 A TW 92125231A TW I243186 B TWI243186 B TW I243186B
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polyimide film
acid
aromatic
diamine
component
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TW092125231A
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Chinese (zh)
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TW200420618A (en
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Hisayasu Kaneshiro
Takaaki Matsuwaki
Kiyokazu Akahori
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Kaneka Corp
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    • 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
    • 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
    • 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
    • B29C41/00Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
    • B29C41/02Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of definite length, i.e. discrete articles
    • B29C41/12Spreading-out the material on a substrate, e.g. on the surface of a liquid
    • 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
    • B32B15/08Layered 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 of synthetic resin
    • B32B15/088Layered 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 of synthetic resin comprising polyamides
    • 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
    • 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
    • C08G73/1003Preparatory processes
    • C08G73/1007Preparatory processes from tetracarboxylic acids or derivatives and diamines
    • 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
    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05KPRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K1/00Printed circuits
    • H05K1/02Details
    • H05K1/03Use of materials for the substrate

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Polymers & Plastics (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Materials Engineering (AREA)
  • Microelectronics & Electronic Packaging (AREA)
  • Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)

Abstract

This invention relates to a kind of polyimide film, which comprises 3,3',4,4'-benzophenonetetracarboxylic dianhydride and can satisfy physical properties such as mean linear expansion coefficient between 100 and 200 DEG C being above 18 ppm/DEG C and below 28 ppm/DEG C, elastic modulus being greater than 4.5 GPa, and coefficient of expansion caused by moisture absorption being below 13 ppm. Due to fulfilling all of the three physical property requirements, the polyimide film which prevents warping or curling from occurring in the TAB tape and flexile printed circuit board processing steps can be realized.

Description

1243186 玖、發明說明: 【發明所屬之技術領域】 伴隨各式各樣之電子機器之輕量、小型化,聚醯亞胺膜 吊用以作為絕緣材料,本發明係關於聚醯亞胺膜、該聚醯 亞胺膜之製造方法,及其利用代表性之一例。特別關於被 加工為撓性印刷電路板(Fiexible printed wiring board)及帶 自動接合技術方式(Tape Automated Bonding, TAB)帶之基 膜而使用之聚醯亞胺膜、及其製造方法、利用一例者。 【先前技術】 先前,撓性印刷基板(簡WFPC)係活用其柔韌性,主要被 指®使用於照相機内部之狹窄之空間。然而,近幾年FPC 於軟式磁碟機(FDD)、硬式磁碟機(HDD)、影印機、印刷機 等之驅動器部分亦廣泛地被使用,而被尋求更加提高FPC 之摺動彎曲特性。 FPC樹脂膜作為基礎,該樹脂膜亦稱為基膜。作為該基 膜若其目的為使之提高摺動性及彎曲性,使用由化學結 構上、f曲性高之聚醯亞胺組成之聚醯亞胺膜即可。 於此作為上述聚醯亞胺膜,具各式各樣之物性者被開 發,特別是於藉帶自動接合技術方式(TAB方式為略記)之 FPC之加工步驟中,作為基膜使用之聚醯亞胺膜,被尋求具 備其次表示之3種物性者。 (1)適度之熱膨脹性 一般幫曲性高之聚醯亞胺因為熱膨脹性高,即因線膨脹 係數大’作為基膜使用聚酸亞胺膜之FPC具有產生彎曲及捲1243186 发明 Description of the invention: [Technical field to which the invention belongs] With the lightweight and miniaturization of various electronic devices, polyimide film hanging is used as an insulating material. The present invention relates to polyimide film, A representative example of a method for producing the polyfluoreneimide film and its use. In particular, a polyimide film used for processing into a flexible printed wiring board (Fiexible printed wiring board) and a base film with a Tape Automated Bonding (TAB) tape, a method for manufacturing the same, and an example of use . [Previous technology] Previously, flexible printed circuit boards (WFPC) used its flexibility and were mainly referred to as ® used in narrow spaces inside cameras. However, in recent years, FPC has been widely used in the drive parts of flexible disk drives (FDD), hard disk drives (HDD), photocopiers, printing machines, etc., and it is sought to further improve the flexural bending characteristics of FPC. FPC resin film is used as a base, and this resin film is also called a base film. As the base film, a polyimide film composed of polyimide having high chemical flexibility and high f-flexibility may be used for the purpose of improving the flexibility and bendability. Here, as the above polyimide film, various physical properties have been developed, especially in the processing steps of FPC by using the automatic bonding technology method (TAB method is abbreviated), as a polymer film used as a base film. The imine film is sought for those who have the following three physical properties. (1) Moderate thermal expansion Polyimide with high flexibility is generally high in thermal expansion, that is, it has a large linear expansion coefficient. 'FPC using polyimide film as the base film has bending and curling.

O:\87\87969-940216.DOC -6 - 1243186 曲等缺點。再者,若反過來選擇線膨脹係數小之聚醯亞胺 而开y成树月曰膜,將該作為基膜而使用,因失去帶本身之撓 性,基膜變成非常脆弱,導致連所得之FPC之彎曲性亦降低 之缺點。 但疋’近幾年上述TAB方式作為能對應半導體設備之多 凡化、小型化、高密度封裝之技術而輩受關注。於tab方 式,设置為了於連續成片之樹脂膜載置LSI等之半導體晶片 之孔(儀器孔),於其上形成非常薄之銅箔導線,介該銅箔導 線連接LSI等及印刷電路板等。於TAB方式中,一般使用由 保護層、黏著劑層及有機絕緣膜層(基片層)之3層結構所構 成之覆晶接合帶(略記為FC帶)。 作為加工上述FC帶使用TAB方式之TAB帶,其加工步驟 一般由其次之8個步驟構成。即,①於FC帶根據穿孔形成為 了載置帶搬送用之鏈輪孔及半導體晶片之步驟,②除去保 濩層銅箔黏合之後,硬化黏著劑之步驟(銅箔積層步驟),③ 根據塗上絕緣塗料進行蝕刻且剝離絕緣塗料,形成銅箔預 定之圖形(配置圖形)之步驟(配置圖形形成步驟),④金屬鍍 層處理步驟,⑤半導體接合步驟,⑥樹脂封裝步驟,⑦穿 孔步驟,及⑧外引腳接合步驟之各步驟。經過此般之加工 γ驟,於TAB贡封裝LSI等。再者,經過上述②之步驟之後 所付之層$體稱之為有膠軟式銅箔層疊板(略記為FCcl)。 於上述加工步驟中,產生FCCL或TAB帶之彎曲及捲曲, 此般之彎曲及捲曲,成為引起TAB帶封裝LSI等之時之封裝 不良之敢大原因之一。即,此般之彎曲及捲曲,於尋求尺O: \ 87 \ 87969-940216.DOC -6-1243186. In addition, if polyimide with a small linear expansion coefficient is selected in turn to form a yew film, and this film is used as a base film, the base film becomes very fragile due to the loss of the flexibility of the belt itself, resulting in continuous income. The disadvantage of FPC is that the flexibility is also reduced. However, in recent years, the above-mentioned TAB method has attracted attention as a technology capable of supporting the versatility, miniaturization, and high-density packaging of semiconductor devices. In the tab method, a hole (instrument hole) for mounting a semiconductor wafer such as an LSI on a continuously formed resin film is formed, and a very thin copper foil wire is formed thereon, and the copper foil wire is connected to the LSI and the printed circuit board. Wait. In the TAB method, a flip-chip bonding tape (abbreviated as an FC tape) composed of a three-layer structure of a protective layer, an adhesive layer, and an organic insulating film layer (substrate layer) is generally used. The TAB method is used to process the above-mentioned FC tape, and the processing steps are generally composed of the next 8 steps. That is, ① the step of forming a sprocket hole and a semiconductor wafer for carrying the tape on the FC tape according to the perforation, ② a step of removing the adhesion layer copper foil and then hardening the adhesive (copper foil lamination step), ③ according to the coating The step of etching the insulating coating and peeling the insulating coating to form a predetermined pattern (configuration pattern) of the copper foil (configuration pattern forming step), ④ metal plating processing step, ⑤ semiconductor bonding step, ⑥ resin packaging step, ⑦ perforation step, and各 Each step of the outer pin bonding step. After such processing, the γ step is used to package the LSI in TAB. In addition, the layer to be paid after the above step ② is called an adhesive-soft copper foil laminated board (abbreviated as FCcl). In the above processing steps, bending and curling of the FCCL or TAB tape is generated, and such bending and curling becomes one of the major causes of poor packaging when the TAB tape is used to package the LSI. That is, such bending and curling, in seeking the ruler

〇 Λ87\87969-940216.DOC 1243186 寸精度之步驟引發各式各樣之不良。具 西?要国/ β耶⑶於- -置圖形形成步驟,引起於配置圖形形成銅箔之時之不良 形成⑤於半導體接合步驟或⑥外引腳接合步驟,彡|起半 V體曰曰片之連接不良等。此外,實際之步驟因進行分離元 ^帶式(reeU0_reei),ΤΑΒ帶之較長方向布滿張力。因此兀 犯矯正贡較長方向之彎曲及捲曲,但不能矯正帶幅 之彎曲及捲曲。 向 如此,可說TAB帶及FPC使用之聚醯亞胺膜,具適度之熱 膨脹性者為較佳者,其線膨脹係數產生彎曲及捲曲之程度 _ 不大,再者失去可撓性之程度不小之範圍内者為必要。作 為如此之線膨脹係數之範圍,具體上18 ppm/r以上、^ ppm/°C以下為較佳者。 (2)吸水性吸濕性小 基膜之吸水率大之情況,上述②銅箔積層步驟之後,產 生積蓄内部應力於夾於基膜及銅箔之黏著劑層之問題。該 内α卩應力如同其下一般被積蓄。即,於②銅箔積層步驟, 結束黏著劑之硬化反應,為從硬化用加熱爐取出之後乾燥 基膜,基膜不歪斜地與銅箔固定。於此,若於黏合狀態放 置銅箔,基膜隨時間一起吸濕膨脹。相對於此,銅箔不吸 濕膨脹,並且與帶比較,剛性大之帶之膨脹由於原因亦幾 乎未發生尺寸變化之事。因此,於夾於基膜及銅箔之黏著 劑層積蓄内部應力。 因此’若於该狀怨進行③配置圖形形成步驟,因變成重 複乾煉及吸濕,一旦藉由蝕刻法於銅箔上形成配線圖形, O:\87\87969-940216.DOC -8- 1243186 則銅笛被除去之部分之應力被放出產生尺寸變化。因此, 即使為了形成配線圖形使用光掩膜,既形成較該光掩膜尺 寸大之圖形,亦產生彎曲及捲曲。其結果發生與半導體設 備之連接不良。如此之尺寸變化成為於TAB加工步驟之成 品率降低之原因。〇 Λ87 \ 87969-940216.DOC 1243186 inch precision steps cause all kinds of defects. With West? The main country / β 耶 ⑶ in the--pattern formation step, caused by the formation of the pattern formation of copper foil defective formation ⑤ in the semiconductor bonding step or ⑥ outer pin bonding step, 彡 | from the V-body connection Bad etc. In addition, since the actual step is performed by the separation element (reeU0_reei), the longer direction of the TAB band is full of tension. Therefore, the offender can correct the bending and curling in the long direction, but cannot correct the bending and curling of the web width. In this way, it can be said that the polyimide film used for TAB tape and FPC has a moderate thermal expansion property, and the degree of bending and curling of its linear expansion coefficient is not large. Within a small range is necessary. As such a range of the linear expansion coefficient, specifically 18 ppm / r or more and ^ ppm / ° C or less is preferable. (2) In the case where the water absorption rate of the base film is small and the water absorption rate of the base film is large, after the above-mentioned ② copper foil lamination step, the problem of accumulating internal stress in the adhesive layer sandwiched between the base film and the copper foil occurs. This internal α 卩 stress is accumulated as it is below. That is, in the step ② copper foil lamination, the hardening reaction of the adhesive is ended, and the base film is dried after being taken out from the hardening heating furnace, and the base film is fixed to the copper foil without skewing. Here, if the copper foil is placed in a bonded state, the base film swells with time with moisture absorption. On the other hand, copper foil does not absorb moisture and swell, and the expansion of a rigid band has almost no dimensional change due to the reason. Therefore, internal stress is accumulated in the adhesive layer sandwiched between the base film and the copper foil. Therefore, if the configuration pattern forming step is performed in this situation, it will become repeated drying and moisture absorption. Once the wiring pattern is formed on the copper foil by etching, O: \ 87 \ 87969-940216.DOC -8- 1243186 Then the stress of the removed part of the copper flute is released to produce a dimensional change. Therefore, even if a photomask is used to form a wiring pattern, a pattern larger than the size of the photomask is formed, and bending and curling are also generated. As a result, a poor connection with the semiconductor device occurred. Such a dimensional change causes a reduction in the yield of the TAB processing step.

如此’對基膜要求低吸水吸濕性。因此,為了於對TAB 帶及FPC之加工中,不使其產生上述之彎曲及捲曲之不適, 適度之範圍内之線膨脹係數及吸濕膨脹係數小之基膜成為 必要。 (3)彈性模數 並且基膜之彈性模數小,即彈性弱,亦具基膜產生尺寸 變化之情況。此係因分離元件帶式之製造步驟中,較長方 向布滿張力。該尺寸變化對加工步驟帶來不良影響,成為 ’考曲及捲曲之原因。因此,譬如使用於TAB帶之聚醯亞胺 膜’具彈性模數大者之必要。 然而,若基膜之彈性模數變大,則衍生線膨脹係數小之 問題。此係因彈性模數及線膨脹係數大大地依存於聚醯亞 月女之_人化學結構(反覆單元之結構)。即,一般選擇如同彈 性杈數變大之聚醯亞胺之一次化學結構的情況,線膨脹係 數菱小,失去聚醯亞胺膜之可撓性而彎曲性下降。 如同上述一般,為了於FPC藉由TAB方式加工之步驟,不 發生彎曲及捲曲,尋求能取得(1)熱膨脹性及(2)吸水吸濕性 及(3)彈性模數之3個物性調合之聚醯亞胺膜。 於此,於日本公開專利公報r特開平9_328544」(公開曰: 〇 :\87\87969-940216.D0C -9- 1243186 1997年12月22日),聚醯亞胺膜被明確指示,其由作為酸成 分使用3,3f,4,4^二苯甲酮四羧酸二酐所得之聚醯亞胺組成 之’該聚酿亞胺膜,被報告具有「略低之吸水性、略低之 吸濕膨脹係數、高彈性模數」及「低熱膨脹係數」(譬如參 照段落號碼〔0059〕)。該公報中被報告之聚醯亞胺膜係作 為酸成分使用焦苯六甲酸二酐或3,31,4,4’-二苯甲_四魏酸 一酐,作為二胺成分對苯二胺使用4,4’ -氧雙苯胺;使用使 該等酸成分及二胺成分共聚之聚醯亞胺而被形成。 然而,使用於上述之公報所報告之聚醯亞胺膜,實際上 即使可取得(1)熱膨脹性及(3)彈性模數之調合,仍產生(2) 吸水吸濕性惡劣之問題。具體上,被記載於上述公報之實 施例之吸水率為2.62〜3.69%之範圍内與吸濕膨脹係數為 16· 8〜29· 8 ppm之範圍内變得非常大。 再者,於日本公開專利公報「特開平、235373」(公開曰: 1997年9月9日),「聚酿亞胺之塊成分由剛結構之芳香 族一胺化a物與芳香族四羧酸類化合物組成及共聚作用聚 1亞胺之任思成分,其由柔性結構之芳香族二胺化合物與 至/ 2種方香族四羧酸類化合物組成,分子結合而成之共聚 作用k醯亞胺」明確指示,作為酸成分使用3,3,,4,4,_二笨甲 納四窥酸二酐之例被明確指示(參照同公報之實施例5)。 ^述A報中,作為可得之「樹脂形成體、兼具高彈性 杈數、低熱膨脹性、低吸收性」。確實使用3,3,,44,_二笨甲 ’四…肝之實施例11,彈性模數為4:3’ GPa(440 g )、線私脹係數為16.7 Ppm/°C、吸水率變成2·4%,確In this way, the base film is required to have low water absorption and moisture absorption. Therefore, in order to prevent the above-mentioned bending and curling discomfort during processing of TAB tapes and FPCs, a base film with a small linear expansion coefficient and a low hygroscopic expansion coefficient in a moderate range is necessary. (3) Elastic modulus And the elastic modulus of the base film is small, that is, the elasticity is weak, and there may be a case where the base film has a dimensional change. This is because the tension is applied in the longer direction in the manufacturing step of the separation element tape. This dimensional change has an adverse effect on the processing steps and becomes the cause of 'curving and curling.' Therefore, for example, a polyimide film 'used in a TAB tape has a large elastic modulus. However, if the elastic modulus of the base film becomes large, a problem arises that the coefficient of linear expansion is small. This is because the modulus of elasticity and the coefficient of linear expansion greatly depend on the chemical structure of the human being (the structure of the repeated unit). That is, the primary chemical structure of polyimide, which has a large number of elastic branches, is generally selected, the linear expansion coefficient is small, the flexibility of the polyimide film is lost, and the flexibility is reduced. As above, in order to avoid bending and curling in the process of FPC by TAB method, seek to obtain 3 physical properties of (1) thermal expansion and (2) water and moisture absorption and (3) elastic modulus. Polyimide film. Here, in Japanese Patent Laid-Open Publication No. Hei 9-328544 "(publication: 〇: \ 87 \ 87969-940216.D0C -9-1243186 December 22, 1997), the polyimide film was explicitly instructed by The polyimide film composed of polyimide obtained by using 3,3f, 4,4 ^ benzophenonetetracarboxylic dianhydride as the acid component is reported to have a "slightly lower water absorption, slightly lower Moisture expansion coefficient, high elastic modulus "and" low thermal expansion coefficient "(for example, refer to paragraph number [0059]). The polyimide film reported in this bulletin uses pyromellitic dianhydride or 3,31,4,4'-dibenzo-tetraweilic acid monoanhydride as the acid component, and p-phenylenediamine as the diamine component. 4,4'-oxybisaniline is used; polyimide is used to copolymerize the acid component and the diamine component. However, even if the polyimide film reported in the above publication is used, (1) the combination of thermal expansion properties and (3) the elastic modulus can still cause (2) the problem of poor water and moisture absorption. Specifically, the examples described in the above-mentioned publications have extremely large water absorption ratios ranging from 2.62 to 3.69% and hygroscopic expansion coefficients ranging from 16 · 8 to 29 · 8 ppm. Furthermore, in Japanese Published Patent Publication "Japanese Patent Laid-Open No. 235373" (publication: September 9, 1997), "the block component of polyimide is composed of an aromatic mono-aminated compound and an aromatic tetracarboxylic compound having a rigid structure. Composition of acid compounds and copolymerization of any component of polyimine, which is composed of an aromatic diamine compound with a flexible structure and up to 2 kinds of aromatic tetracarboxylic acid compounds, and is a copolymerization effect of the molecular combination "It is clearly instructed that the use of 3,3,4,4, _dibenzylidene tetrapic acid dianhydride as an acid component is clearly instructed (refer to Example 5 of the same publication). ^ In the A report, as a "resin-formed product, it has both high elasticity, low thermal expansion, and low absorption". Indeed using 3,3,, 44, _ two stupid armor 'four ... liver Example 11, the elastic modulus is 4: 3' GPa (440 g), the linear inflation coefficient is 16.7 Ppm / ° C, the water absorption rate becomes 2.4%, indeed

O:\87\87969-940216.DOC -10- 1243186 實⑴-(3)之各物性雖然提高,但為使用藉由上述Μ方& FPCH如同表示於後述之比較例8,仍無法稱為充分。 如此’於作為聚醯亞胺之酸成分使用3,3’,4,_二苯甲酮四O: \ 87 \ 87969-940216.DOC -10- 1243186 Although the physical properties of ⑴- (3) are improved, the above-mentioned M-side & FPCH is used as Comparative Example 8 described below, which cannot be called full. In this way, 3,3 ', 4, _benzophenone tetra is used as an acid component of polyimide.

㈣-酐所传之聚醯亞胺財,先前特別是使用藉由TAB 方式之FPC(TAB帶等)之情況,同時能實現藉由熱之膨脹、 吸水吸濕性、彈性模數之所謂該諸物性為較佳者者係習知 者。然而’評價上述諸物性之時,與其說使用⑴線膨服係 數、⑺吸濕膨脹係數及晴性模數,不如使用具體之參 數,關㈣等參數作為全部理想之範圍之值者未被習知, 再者將該等⑴〜(3)之參數之數值調整作為全部理想之範 圍之值乃非常困難者。 【發明内容】 本發明係㈣上述之問題而做出者,其目的特別是作為 用於TAB帶及FPC之基膜,於使用利用3,3,,从二苯甲綱四 缓酸二酐所得之㈣亞賴之情況,可充分地取得⑴熱膨 脹性、(2)吸水吸濕性、及(3)彈性模數之調和,提供能更有 效迴避彎曲及捲曲之發生之聚醯亞胺膜及其製造方法、其 利用之代表性之一例。 μ 於此,本發明者鑑於上述問題點銳意討論之結果,特別 為了評價⑺吸水吸濕性而使用吸濕膨脹係數,充分地取得 (1)熱膨脹性、(2)吸水吸濕性、及(3)彈性模數之各物性之調 合成為可&,其結果滿足能製造可更有效迴避彎曲及捲曲 之發生之聚醯亞胺膜,達到完成本發明。取得該等(ι)〜(3) 之各物性之調合之聚醯亞胺膜,使用作為代表性之一例之 O:\87\87969-940216.DOC -11 - 1243186 TAB帶’當然應用於多樣之用途之Fpc亦能適宜地使用。 即,關於本發明之㈣亞胺膜,為了解決上述之問題, 作為主要由方香族二胺與芳香族四羧酸二酐合成之聚醯胺 酉夂所得之水醯亞胺膜’ &1〇〇_2〇〇。。之平均線膨脹係數為 ppm ’彈性模數為4·5咖以上,吸濕膨脹係數為^ ppm以下,作為芳香族四羧酸二酐,使用3,3,,4,4,_二苯甲酮 四羧酸二酐作為必要成分而構成。 於關於本發明之聚醯亞胺冑中,纟芳錢四叛酸二肝成 分作為100 mol%之時,使用3,3,,4,4,_二苯甲酮四羧酸二酐 如同20〜60 mol%之範圍内為較佳者。 此外’作為關於本發明之聚醯亞胺膜中所用之酸成分, 使用表示於其次之化合物為較佳者。#,作為⑴上述芳香 族四羧酸二酐成分,使用芳香族酯酸二酐為較佳者。再者, (II)上述全芳香族四羧酸二酐成分作為100m〇l%之時,使用 上述芳香族酯酸二酐如同為10〜60 mol%之範圍内為較佳 者。更且,作為(ΠΙ)上述芳香族酯酸二酐,使用對伸苯基 雙(偏苯三酸單酯酐)為較佳者。 作為於關於本發明之聚醯亞胺膜中所用之二胺成分,使 用直線性二胺及彎曲性二胺各自至少丨種為較佳者。此時, 全芳香族二胺成分作為1〇〇 m〇l%之時,使用上述直線性二 胺及彎曲性二胺各自於20〜80 mol%之範圍内及80〜20 m〇l%之範圍内為較佳者。(π)作為上述直線性二胺,使用 對苯二胺為較佳者。(ΠΙ)再者,作為上述彎曲性二胺,使 用4,4’-氧雙苯胺為較佳者。 O:\87\87969-940216.DOC -12- 1243186 於關於本發明之聚醯亞胺膜中’上述直線性二胺及彎曲 性一胺於聚醯亞胺分子中,任意分佈為較佳者。 關於本發明之㈣亞胺膜之製造方法,上述㈣亞胺膜 之構成至少包含a)於有機溶劑申,使芳香族二胺及芳香族 四羧酸二酐聚醯胺酸反應而得聚醯胺酸溶液之步驟,…於 支持體上洗#包含i $㈣胺酉曼溶液之製膜黏祠劑之步 驟,c)於支持體上加熱上述製膜黏稠劑之後,從支持體拆 離凝膠膜之步驟,d)更且加熱凝膠膜,醯亞胺化殘存之胺 酸,使之乾燥之步驟, 於關於本發明之聚醯亞胺膜之製造方法中,至少併用脫 水劑及醯亞胺化觸媒為較佳者。 作為關於本發明之聚醯亞胺膜之利用之一例,可舉出於 上述聚醯亞胺膜上設置黏著劑層及保護層而成iFc帶、至 少具有由上述聚醯亞胺膜組成之層及金屬導電層之軟性印 刷電路板。 若根據上述構成,特別是作為用於TAB帶及即之基膜, 於使用3,3’,4,4’-二苯甲酮四羧酸二酐作為必要成分所得之 聚醯亞胺膜之情況,同時如同未發生彎曲和卷曲一般兼備 線膨賬係數和彈性模數,提供亦不發生以吸濕之尺寸變化 作為原因之彎曲及卷曲之聚醯亞胺膜成為可能。 本發明更進一步之其他目的、特徵及優異點,根據表示 於以下之記載可充分明白。 【實施方式】 若說明關於本發明之實施之一形態,則如同於下之。再 O:\87\87969-940216.DOC -13- 1243186 者,本發明並非被限定於該者。以下, ^ M下,關於本發明之詳細, 聚醯亞胺膜、其製造方法、其利用 八〜用 以具體之實施例之順 序具體說明。 (1)關於本發明之聚醯亞胺膜 <聚醯亞胺膜之物性> 關於本發明之聚醯亞胺膜主要是醯亞胺化由芳香族四羧 酸二酐及芳香族二胺合成之聚醯胺酸(p咖micac⑷,使用 聚醯亞胺而成者。該期間,上述芳香族四羧酸二酐中,至 少3有3,3,4,4 - 一苯甲酮四羧酸二酐,如此所得之聚醯亞胺 膜成為滿足其次表示之3個條件。 條件(1) ·於從100C至200°C之平均線膨脹係數為18〜28 ppmrc之範圍内。 條件(2) ··彈性模數為4.5 GPa以上。 條件(3):吸濕膨脹係數為13 ppm以下。 上述來S&亞胺膜’根據滿足條件(i),作為FPC及tab帶 被使用時,彎曲及捲曲之發生被防止。據此,彎曲性高之 同時,線膨脹係數亦高,不產生彎曲及捲曲之範圍内之聚 醯亞胺膜之供給成為可能。再者,較上述聚醯亞胺膜之從 100 C至200°C之平均線膨脹係數理想之範圍為18 ρριη〜25 ppm/°C之範圍内,更加理想之範圍為2〇〜25 ppm/tt之範圍 内。 同時’上述聚醯亞胺膜根據滿足條件(2),於分離元件帶 式之製造步驟之尺寸變化,進而防止FPC及TAB帶之彎曲及 捲曲之發生。再者,較上述聚醯亞胺膜之彈性模數理想之 O:\87\87969-940216.DOC -14- 1243186 範圍為4.5 0?&〜8.0 0?3之範圍内,更加理想之範圍為5〇 GPa〜7.5 GPa之範圍内。 並且,上述聚酸亞胺膜根據滿足條件(3),藉由吸濕膨脹, 銅癌間内部應力之尺寸變化被防止。再者,較上述聚醯亞 胺膜之吸濕膨脹係數理想之範圍為12 ppm以下,更加理想 之fe圍為11 ppm以下。 關於本發明之聚醯亞胺膜,根據滿足上述3個之條件,兼 有不發生彎曲及捲曲一般之熱膨脹性及彈性模數之同時, 使吸水吸濕性降低成為可能,提供亦不發生以吸濕之尺寸 變化作為原因之彎曲及捲曲之聚醯亞胺膜成為可能。 <用於聚醯亞胺之合成之單體成分> 關於本發明之聚醯亞胺膜,主要是使用根據醯亞胺化由 芳香族四羧酸二酐及芳香族二胺合成之聚醯胺酸 acid)所得之聚醯亞胺。即,於本發明所用之聚醯亞胺,前 驅體之聚醯胺酸聚合(合成)之後,可藉由醯亞胺化其之而庐 得。 於此,所謂上述所言之「主要是由芳香族二胺與芳香族 四羧酸二酐合成之聚醯胺酸」,指在作為聚醯胺酸之原料之 酸成分之中,芳香族四羧酸二酐之含有比率最大,二胺成 刀之中芳香族二胺之含有比率最大之情況者。 換句話說,於本發明中,於作為前驅體之聚醯胺酸之聚 合,作為酸成分含有芳香族四羧酸二酐,作為二胺成分含 有芳香族二胺,若該等成分最大使用為佳,亦可用其他之 酸成分及二胺成分。 O:\87\87969-940216.DOC -15- 1243186 以下,具體說明關於作為聚醯胺酸之原料(單體成分)之酸 成分及二胺成分。 <酸成分(酸二酐成分)> 關於本發明裡之聚醯亞胺膜,聚醯亞胺之前驅體之聚醯 胺酸之原料之中,作為酸成分至少能使用3,3f,4,4,-二苯甲酮 四羧酸二酐。該3,3,,4,4,-二苯甲酮四羧酸二酐,包含於上述 芳香族四羧酸二酐之範疇者。 聚合聚醯胺酸的情況,作為酸成分使用上述3,3,,4,4,-二苯 曱鋼四羧酸二酐之情況之具體量(使用的劑量)並非特別被 限定者,然而全芳香族四羧酸二酐成分作為1〇〇 mol%之情 况’若於20〜60 mol%之範圍内使用為較佳者,於25〜60 m〇l%之範圍内被使用更理想,於25〜55 mol%則更加理 想。換句話說,3,3,,4,4’-二苯甲酮四羧酸二酐之使用量之上 限較L為60 mol%以下,更較佳為55 mol%以下。同時, 下限較佳為20 mol%以上,更較佳為25 mol%以上。 根據3,3,,4,4,-二苯甲酮四羧酸二酐之使用量於該範圍 内,適宜取得線膨脹係數及彈性模數之調合者成為可能, 根據該範圍於上限以下,使吸濕膨服係數小者成為可能。 丹考,作為於本發明使用之上述芳香族四羧酸二酐, 2上述3,3’,4,4’-二苯甲酮四羧酸二酐之外,更且再者加』 香知酿酸二酐為較佳者。於此所謂之「芳香賴酸二酐 作為指向於結構中含酯之芳香族四羧酸酸二酐。 作為上述芳香族醋酸二酐’並非特 體之—例能舉出對伸苯基雙(偏苯三酸單酯^乙^In the case of polyimide properties transmitted by hydrazone-anhydride, the use of FPC (TAB tape, etc.) by the TAB method has previously been achieved. At the same time, it can achieve the so-called due to thermal expansion, water absorption and moisture absorption, and elastic modulus. Those whose physical properties are better are those who know. However, when evaluating the above-mentioned physical properties, rather than using the linear expansion coefficient, hygroscopic expansion coefficient, and sunny modulus, it is better to use specific parameters, such as parameters, as the values of all the ideal ranges. It is known that it is very difficult to adjust the numerical values of the parameters (1) to (3) as the values of all the ideal ranges. [Summary of the Invention] The present invention was made based on the above-mentioned problems, and its purpose is particularly as a base film for TAB tape and FPC, using 3,3, obtained from dibenzoyltetracarboxylic acid dianhydride. In the case of Yalai, it is possible to fully obtain the reconciliation of thermal expansion, (2) water absorption and moisture absorption, and (3) elastic modulus, and provide polyimide film and A typical example of its production method and its use. μ Here, in view of the results of the intensive discussion in view of the above-mentioned problems, the inventors have used a hygroscopic expansion coefficient in particular to evaluate the hygroscopicity and hygroscopicity, and have sufficiently obtained (1) thermal expansion properties, (2) hydroscopic properties and ( 3) The adjustment of the various physical properties of the elastic modulus is &, and the result satisfies that it is possible to manufacture a polyimide film which can more effectively avoid the occurrence of bending and curling, and complete the present invention. The polyimide film obtained by blending each of these physical properties (ι) to (3) is used as a representative example: O: \ 87 \ 87969-940216.DOC -11-1243186 TAB tape is of course applied to a variety of Fpc for the purpose can also be used suitably. That is, in order to solve the above-mentioned problems, the ammonium imine film of the present invention is a hydroimide film obtained from polyammonium amine mainly composed of an aromatic diamine and an aromatic tetracarboxylic dianhydride. 100〇_2〇〇. . The average linear expansion coefficient is ppm 'The elastic modulus is 4.5 or more, and the hygroscopic expansion coefficient is ^ ppm or less. As the aromatic tetracarboxylic dianhydride, 3,3,, 4,4, _benzoyl Ketone tetracarboxylic dianhydride is constituted as an essential component. In the polyimide according to the present invention, when the content of the diliverium tetrametanoic acid dihepatic acid component is 100 mol%, 3,3,, 4,4, _benzophenonetetracarboxylic dianhydride is used as 20 A range of ~ 60 mol% is preferred. In addition, as the acid component used in the polyfluorene imide film of the present invention, it is preferable to use the compound shown next. #, It is preferable to use an aromatic ester acid dianhydride as the aromatic tetracarboxylic dianhydride component. When (II) the total aromatic tetracarboxylic dianhydride component is 100 mol%, it is preferable to use the aromatic ester acid dianhydride in the range of 10 to 60 mol%. Furthermore, as (III) the aromatic ester acid dianhydride, p-phenylene bis (trimellitic acid monoester anhydride) is preferably used. As the diamine component used in the polyfluorene imine film of the present invention, it is preferable to use at least one of each of a linear diamine and a flexible diamine. At this time, when the wholly aromatic diamine component is 100 mol%, the linear diamine and the flexible diamine described above are each used in the range of 20 to 80 mol% and 80 to 20 mol%. Within the range is better. (Π) As the linear diamine, p-phenylenediamine is preferably used. (II) As the flexible diamine, 4,4'-oxybisaniline is preferably used. O: \ 87 \ 87969-940216.DOC -12-1243186 In the polyimide film of the present invention, the above-mentioned linear diamine and bendable monoamine are distributed in the polyimide molecule, and the arbitrary distribution is better. . With regard to the method for producing a fluorene imine film according to the present invention, the structure of the fluorene imine film includes at least a) an organic solvent and reacting an aromatic diamine and an aromatic tetracarboxylic dianhydride polyfluorinated acid to obtain polyfluorene. Steps of amino acid solution, ... washing on the support #including the steps of film forming adhesive agent containing ㈣amine 酉 mann solution, c) after heating the film forming viscosity agent on the support, detaching the coagulation from the support The step of the gel film, d) heating the gel film, and the step of drying the imine remaining amine acid and drying it. In the method for manufacturing the polyfluorine film of the present invention, at least a dehydrating agent and An imidization catalyst is preferred. As an example of the use of the polyfluorene imide film of the present invention, an iFc band formed by providing an adhesive layer and a protective layer on the polyfluorine imide film, and at least a layer composed of the polyfluorine imide film may be mentioned. And a flexible printed circuit board with a metal conductive layer. According to the above structure, especially as a base film for a TAB tape, that is, a polyimide film obtained by using 3,3 ', 4,4'-benzophenonetetracarboxylic dianhydride as an essential component In this case, it is possible to provide a polyimide film having no linear expansion coefficient and elastic modulus at the same time as no bending and curling, and no bending or curling due to dimensional changes in moisture absorption. Still other objects, features, and advantages of the present invention will be fully understood from the following description. [Embodiment] If one embodiment of the present invention is described, it is the same as the following. O: \ 87 \ 87969-940216.DOC -13-1243186, the present invention is not limited to this. In the following, the details of the present invention, the polyimide film, its manufacturing method, and its use will be described in detail in the order of specific examples. (1) Polyimide film of the present invention < Physical properties of polyimide film > About the polyimide film of the present invention is mainly amidated by aromatic tetracarboxylic dianhydride and aromatic dicarboxylic acid. Polyacrylic acid synthesized by amines (caffeic acid), produced using polyimide. During this period, at least 3 of the aromatic tetracarboxylic dianhydrides mentioned above had 3,3,4,4-benzophenone tetra Carboxylic dianhydride, the polyimide film thus obtained meets the following three requirements. Condition (1): Within the range of an average linear expansion coefficient from 100C to 200 ° C is 18 to 28 ppmrc. Conditions ( 2) The elastic modulus is 4.5 GPa or more. Condition (3): The coefficient of hygroscopic expansion is 13 ppm or less. When the S & imine film is used as FPC and tab tape according to the condition (i), The occurrence of bending and curling is prevented. According to this, at the same time of high bending property, the linear expansion coefficient is also high, and it is possible to supply polyimide film within the range that does not cause bending and curling. Furthermore, compared with the above-mentioned polyimide The ideal linear expansion coefficient of the amine film from 100 C to 200 ° C is in the range of 18 ρριη ~ 25 ppm / ° C, and more The ideal range is within the range of 20 to 25 ppm / tt. At the same time, according to the above condition (2), the polyimide film has a dimensional change in the manufacturing step of the separation device tape type, thereby preventing bending of the FPC and TAB tapes. And the occurrence of curling. Furthermore, the elastic modulus of the polyimide film is more ideal than O: \ 87 \ 87969-940216.DOC -14-1243186 in the range of 4.5 0? &Amp; ~ 8.0 0? 3 A more desirable range is 50 GPa to 7.5 GPa. In addition, the polyimide film satisfies the condition (3), and the dimensional change of internal stress between copper cancers is prevented by hygroscopic expansion according to the condition (3). Furthermore, The ideal range for the hygroscopic expansion coefficient of the polyimide film is 12 ppm or less, and the more desirable fe range is 11 ppm or less. Regarding the polyimide film of the present invention, according to the above three conditions, It has the general thermal expansion properties and elastic modulus without bending and curling, and it is possible to reduce the water absorption and moisture absorption, and it is possible to provide a polyimide film that does not bend and curl due to the dimensional change of moisture absorption. ≪ For the synthesis of polyimide Body composition > on polyimide film of the present invention, mainly using the polyamide acid of the acid (PEI) synthesis from an aromatic tetracarboxylic dianhydride and aromatic diamine) of the resulting polyimide. That is, after the polyimide used in the present invention is polymerized (synthesized) with the polyamic acid of the precursor, it can be obtained by the imidization. Here, the so-called "polyamino acid mainly composed of aromatic diamine and aromatic tetracarboxylic dianhydride" refers to the aromatic four Carboxylic dianhydride has the largest content ratio, and among the diamines, the aromatic diamine has the largest content ratio. In other words, in the present invention, in the polymerization of polyamic acid as a precursor, an aromatic tetracarboxylic dianhydride is contained as an acid component, and an aromatic diamine is contained as a diamine component. It is also good to use other acid components and diamine components. O: \ 87 \ 87969-940216.DOC -15-1243186 The following specifically describes the acid component and diamine component as raw materials (monomer components) of polyamic acid. < Acid component (acid dianhydride component) > Regarding the polyimide film in the present invention, among the raw materials of polyimide of the precursor of polyimide, at least 3,3f can be used as the acid component. 4,4, -benzophenone tetracarboxylic dianhydride. The 3,3,4,4, -benzophenone tetracarboxylic dianhydride is included in the category of the aromatic tetracarboxylic dianhydride. In the case of polymerizing polyamic acid, the specific amount (dose used) in the case of using the above 3,3,4,4, -diphenylphosphonium tetracarboxylic dianhydride as the acid component is not particularly limited, but all When the aromatic tetracarboxylic dianhydride component is 100 mol%, it is better to use it within the range of 20 to 60 mol%, and it is more desirable to use it within the range of 25 to 60 mol%. 25 to 55 mol% is more desirable. In other words, the upper limit of the amount of 3,3,4,4'-benzophenonetetracarboxylic dianhydride is 60 mol% or less, and more preferably 55 mol% or less. Meanwhile, the lower limit is preferably 20 mol% or more, and more preferably 25 mol% or more. According to the usage of 3,3,4,4, -benzophenonetetracarboxylic dianhydride within this range, it is possible to obtain a blend of linear expansion coefficient and elastic modulus, and according to this range, it is below the upper limit. This makes it possible to have a small moisture absorption swelling coefficient. Dan Kao, as the above-mentioned aromatic tetracarboxylic dianhydride used in the present invention, 2 and the above 3,3 ', 4,4'-benzophenone tetracarboxylic dianhydride, and further added " Acid dianhydride is preferred. The so-called "aromatic lysine dianhydride" refers to an aromatic tetracarboxylic acid dianhydride containing an ester in the structure. The above-mentioned aromatic acetic dianhydride is not a specific one—for example, p-phenylene bis ( Trimellitic acid monoester ^ ethyl ^

O:\87\87969-940216_DOC -16- 1243186 苯三酸單酯酐)、雙石炭酸A雙(偏苯三酸單酯酐)等。 上述芳香族酯酸二酐之使用量,並非特別被限定者,然 而若於把全芳香族四羧酸二酐成分作為1〇〇 mol%時,1〇〜 60 mol%之範圍内為較佳者,2〇〜55 md%之範圍内更理 想’ 25〜50 m〇l%之範圍内更加理想。換句話說,芳香族酯 酉欠一酐之使用量之上限,較佳為6〇 m〇l%以下,更較佳為55 mol%以下,更加較佳為5〇 m〇i%以下。同時,下限較佳為 10 mol。/。以上’更較佳為2〇 m〇1%以上,並且更加較佳為25 mol%以上。 根據上述芳香族酯酸二酐之使用量不低於該範圍者,根 據彈性榼數及吸濕膨脹係數之改善效果不很大,超過該範 圍之事獲得柔軟之帶之事成為可能。 於本發明’即使於上述之芳香族S旨酸二肝之中,特別可 理想使用對伸苯基雙(偏苯三酸單酯酐)。據此,能獲得機械 之強度吸濕私脹係數之改善及從熱性行為之觀點中獲得 適宜之聚醯亞胺。 /亥對伸笨基雙(偏笨三酸單酯酐)之使用量亦未特別被限 疋者,不過將全芳香族四羧酸二酐成分作為1〇〇 m〇1%時, 1〇〜60 m〇1%之範圍内為較佳者,20〜55 mol%之範圍内更 理想,25〜50 m〇l%之範圍内更加理想。換句話說,對伸苯 基雙(偏苯三酸單酯酐)之使用量之上限,較佳為6〇m〇i%以 下更較佳為55 mol%以下,更加較佳為5〇 m〇1%以下。同 時,下限較佳為10 m〇l%以上,更較佳為2〇 m〇1%以上,並 且更加較佳為25 mol%以上。O: \ 87 \ 87969-940216_DOC -16-1243186 trimellitic acid monoester anhydride), bis-carbonic acid A bis (trimellitic acid monoester anhydride), etc. The use amount of the above-mentioned aromatic ester acid dianhydride is not particularly limited, but if the total aromatic tetracarboxylic dianhydride component is 100 mol%, it is preferably in the range of 10 to 60 mol%. For example, a range of 20 to 55 md% is more desirable, and a range of 25 to 50 ml% is more desirable. In other words, the upper limit of the amount of the aromatic ester pentane anhydride is preferably 60% or less, more preferably 55% or less, and still more preferably 50% or less. Meanwhile, the lower limit is preferably 10 mol. /. The above 'is more preferably 20 mol% or more, and even more preferably 25 mol% or more. According to the use amount of the above-mentioned aromatic ester acid dianhydride not less than this range, the effect of improving the elastic modulus and the coefficient of hygroscopic expansion is not great, and it is possible to obtain a soft band if it exceeds this range. In the present invention ', even among the above-mentioned aromatic S-acid diliver, p-phenylene bis (trimellitic acid monoester anhydride) is particularly preferably used. According to this, it is possible to obtain an improvement in mechanical strength, moisture absorption, and expansion coefficient, and a suitable polyimide from the viewpoint of thermal behavior. The use amount of phenylbenzylbis (monobenzyltriacid monoester anhydride) is not particularly limited, but when the total aromatic tetracarboxylic dianhydride component is 100%, 1 % A range of from 60 to 60% is more preferred, a range of from 20 to 55 mol% is more preferred, and a range of from 25 to 50% is more desirable. In other words, the upper limit of the amount of p-phenylene bis (trimellitic acid monoester anhydride) used is preferably 60 m% or less, more preferably 55 mol% or less, and more preferably 50 m. 〇1% or less. At the same time, the lower limit is preferably 10 mol% or more, more preferably 20 mol% or more, and even more preferably 25 mol% or more.

O:\87\87969-940216.DOC -17- 1243186 再者,作為於本發明所使用之上述芳香族四羧酸二酐, 使用上述3,3,,4,4,-二笨甲酮四羧酸二酐或是上述3,3,,4,4,_ 二笨曱_四羧酸二酐及上述芳香族酯酸二酐之外,另加上 其他之芳香族四羧酸二酐亦可。所謂於此所言之「之外之 芳香族四羧酸二酐」,作為指向不符合上述3,3,,4,4,_二苯甲 «四幾酸二酐及上述芳香❹旨酸二酐之芳香族四緩酸酸二 酐。 上述其他之芳香族四羧酸二酐,並非特別被限定者,作 為具體之一例,可舉出焦苯六曱酸二酐,2,3,6,7_荼四羧酸 二酐、3,3’,4,4’_聯苯四羧酸二酐、^^,卜荼四羧酸二酐、 2,2’,3,3’_聯苯四羧酸二酐、2,入雙(3,4_聯羧苯基)丙烷二 酐、3,4,9,l〇_peryiene四羧酸二酐、雙〔3,4_聯羧苯基〕丙 烷二酐、1,1-雙(2,3-聯羧苯基)乙烷二酐、込^雙^;聯羧苯 基)乙烷二酐、雙(2,3_聯羧苯基)沼氣二酐、雙(3,4_聯羧苯 基)乙烷二酐、氧聯笨二甲酸二酐、雙(3,‘聯羧笨基)聚砜二 酐、乙烯雙(偏苯三酸單酯酐)、雙石炭酸A雙(偏苯三酸單 醋酐)等。該等單獨使用亦可,組合2種以上使用亦可。 上述其他之芳香族四羧酸二酐中,焦苯六曱酸二酐較 3,3f,4,4f-聯苯四羧酸二酐更可理想使用。 上述其他之芳香族四羧酸二酐之使用量,並非特別被限 定者’然而將全芳香族四羧酸二酐成分作為1〇〇 mol%時, 50 mol%以下為較佳者,45 mol%以下更理想,40 mol%以 下更加理想。換句話說,其他之芳香族四魏酸二酐之使用 里之上限’較佳為5〇 mol%以下,更較佳為45 mol%以下, O:\87\87969-940216.DOC -18- 1243186 更加較佳為40 mol%以下。五土 。丨%以上即可。 再者,下限並非特別被限定者, :據亡:其他之芳香族四羧酸二無水物之使用量於該範 圍内,猎由使用3,3,,4,4,_二芏田⑽ 一本F顯I四羧酸二酐及/或芳 域酸二时,聚醯亞胺膜之改«量效果可變大。 卜於本發明因應對所得之聚醯亞胺膜要求之物性 荨,作為上述酸成分,使用芳香族四錢二野 酐(其他之酸 二酐)亦可一 ,、匕之酉夂二酐之使用量亦非特別被 限定者。 <一胺成分> 於本發明之聚酸亞胺膜,聚酿亞胺之前驅體之聚酸胺酸 之原料之其中’作為二胺成分,至少能制芳香族二胺。 作為上述芳香族二胺,具體上譬如可舉出對苯二胺及其 核置換化合物、聯苯胺及其核置換化合物、4,4,·氧雙苯胺、、 I,3·雙(心胺苯氧)苯、雙(3_胺苯氧)苯、4,4、雙(3僅苯氧) 聯苯、4,4、雙(4-胺笨氧)聯苯、雙(4_(心胺苯氧)笨基)聚石風、 雙(4_(3_胺苯氧)苯基)聚砜、4,4,_二胺二苯基丙烷、4,二 胺二苯基甲烷、4,4,-二胺二苯基硫化物、3,3,_二胺二苯基 聚颯、4,4’-二胺二苯基聚砜、3,3,_氧雙苯胺、3,4,_氧雙苯胺、 2,4’-氧雙苯胺、4,4,-二胺二苯基氧雙苯胺及4,4,_二胺二笨基 矽甲烷、4,4’-二胺二苯乙環氧化磷化氫、4,4,_二胺二苯Ν· 曱基胺、4,4’-二胺二苯基苯基胺、ip二胺笨、I]-二胺 笨等,然而其並非特別被限定者。 於本發明’上述芳香族二胺成分,至少包含直線性O: \ 87 \ 87969-940216.DOC -17-1243186 Furthermore, as the above-mentioned aromatic tetracarboxylic dianhydride used in the present invention, the above-mentioned 3,3,, 4,4, -dibenzone ketone is used Carboxylic dianhydride or 3,3,4,4, _dibenzidine_tetracarboxylic dianhydride and the above aromatic ester acid dianhydride, in addition to other aromatic tetracarboxylic dianhydride can. The so-called "other than aromatic tetracarboxylic dianhydride" mentioned here does not conform to the above 3,3,, 4,4, _dibenzoyl tetrakidic acid dianhydride and the above-mentioned aromatic dicarboxylic acid dianhydride Aromatic tetracarboxylic acid dianhydride. The above-mentioned other aromatic tetracarboxylic dianhydrides are not particularly limited, and specific examples include pyromellitic dianhydride, 2,3,6,7_tetracarboxylic dianhydride, 3, 3 ', 4,4'_biphenyltetracarboxylic dianhydride, ^^, tetracarboxylic dianhydride, 2,2', 3,3'_biphenyltetracarboxylic dianhydride, 2, into bis ( 3,4_bicarboxyphenyl) propane dianhydride, 3,4,9,10_peryiene tetracarboxylic dianhydride, bis [3,4_bicarboxyphenyl] propane dianhydride, 1,1-bis ( 2,3-dicarboxyphenyl) ethane dianhydride, 込 ^ bis ^; bicarboxyphenyl) ethane dianhydride, bis (2,3_dicarboxyphenyl) biogas dianhydride, bis (3,4_ Bis (phenylphenyl) ethane dianhydride, oxydibenzyl dianhydride, bis (3, 'dicarboxybenzyl) polysulfone dianhydride, ethylene bis (trimellitic acid monoester anhydride), biscarbohydrate A bis ( Trimellitic acid monoacetic anhydride) and so on. These may be used alone or in combination of two or more. Among the other aromatic tetracarboxylic dianhydrides mentioned above, pyromellitic dianhydride is more preferable than 3,3f, 4,4f-biphenyltetracarboxylic dianhydride. The use amount of the other aromatic tetracarboxylic dianhydrides is not particularly limited. However, when the total aromatic tetracarboxylic dianhydride component is 100 mol%, 50 mol% or less is preferred, 45 mol. % Is more preferable, and 40 mol% is more preferable. In other words, the upper limit of the use of other aromatic tetraweilic acid dianhydrides is preferably 50 mol% or less, more preferably 45 mol% or less, O: \ 87 \ 87969-940216.DOC -18- 1243186 is more preferably 40 mol% or less. Five soils. Above 丨% is sufficient. Moreover, the lower limit is not particularly limited.: According to the death: the amount of other aromatic tetracarboxylic acid dianhydrous is within this range, hunting by using 3,3,, 4,4, _ 二 芏 田 ⑽ 1 In this case, when the tetracarboxylic dianhydride and / or aromatic acid bis is used, the amount of polyimide film can be increased. According to the present invention, the physical properties of the polyimide film required by the present invention, as the above-mentioned acid component, aromatic tetramethylene dianhydride (other acid dianhydrides) can also be used. The amount used is not particularly limited either. < Monoamine component > In the polyimide film of the present invention, among the raw materials of the polyamic acid precursor of the polyimide precursor, as a diamine component, at least an aromatic diamine can be produced. Specific examples of the aromatic diamine include p-phenylenediamine and its nuclear replacement compound, benzidine and its nuclear replacement compound, 4,4, · oxybisaniline, and I, 3 · bis (cardiamine benzene). Oxygen) benzene, bis (3-aminephenoxy) benzene, 4,4, bis (3 only phenoxy) biphenyl, 4,4, bis (4-aminebenzyloxy) biphenyl, bis (4_ (cardiamine) benzene Oxygen) benzyl) polylithic wind, bis (4- (3-aminephenoxy) phenyl) polysulfone, 4,4, _diaminediphenylpropane, 4, diaminediphenylmethane, 4,4, -Diamine diphenyl sulfide, 3,3, _diamine diphenyl polyfluorene, 4,4'-diamine diphenyl polysulfone, 3,3, _oxybisaniline, 3,4, _oxy Diphenylamine, 2,4'-oxybisaniline, 4,4, -diamine diphenyloxybisaniline and 4,4, _diamine dibenzylsilylmethane, 4,4'-diamine diphenylethyl ring Phosphine oxide, 4,4, _diaminediphenyl N · fluorenylamine, 4,4'-diaminediphenylphenylamine, ipdiaminebenzyl, I] -diaminebenzine, etc., but it is not Specially restricted person. In the present invention ', the aromatic diamine component includes at least linearity

O:\87\87969-940216.DOC -19- 1243186 及彎曲性二胺之一方為較佳者。 、、,於此,所謂上述「直線性二胺」,於主鎖鏈t不含如以乙 醚基1婦基、块丙基、六氟块丙基、幾基、聚硪基、硫 t基等一般之'f曲基,指向2個氨基之氮原子及該等結合之 反原子具排列成一直線之結構之二胺化合物。 作為上述直線性二胺之具體之例,可舉出對苯二胺波及 其核置換化合物、聯苯胺及其核置換化合物等,然而其並 非特別被限定者。上述直線性二胺只使用丨種亦可,適宜地 組合2種以上使用亦可。該等之中尤其使用對苯二胺較為較 佳者。據此’可m、對待性、特性調合之面出色之 聚醯亞胺膜。 再者,所謂上述「彎曲性二胺」,於主鎖鏈中含以乙醚基、 甲烯基快丙基、/、氟块丙基、幾基、减基、硫化基等之 4曲基之一胺,或者不包含彎曲基之情況,指向具2個氨基 之氮原子及與该等結合之碳原子不排列成一直線之結構之 二胺化合物。 作為上述彎曲性二胺之具體之例,可舉出4,4,-氧雙苯 胺、1,3-雙(4-胺苯氧)苯、n —雙(3 一胺苯氧)苯、4,4,-雙(3_ 胺苯氧)聯苯、4,4,-雙(心胺苯氧)聯苯、雙(4-(4-胺苯氧)苯基) 聚砜、雙(4-(3-胺苯氧)苯基)聚颯、4,4,_二胺二苯丙烷、4,4,_ 二胺二苯基甲烧甲烷、4,4,-二胺二苯基硫化、3,3、二胺二 苯基聚硬、4,4’-二胺二笨基聚砜、3,3,_氧雙苯胺、3,4,_氧雙 苯胺、2,4’_氧雙苯胺、4,4,_二胺二苯基二乙及、4,4,_二胺二 苯基石夕曱烧、4,4、二胺二苯乙基磷化氫、4,4,-二胺二苯基O: \ 87 \ 87969-940216.DOC -19-1243186 and one of the flexible diamines are preferred. Here, the so-called "linear diamine" does not contain in the main chain t such as ethyl ether, propyl, hexafluoro, propyl, acetyl, polyfluorenyl, sulfur, etc. In general, the 'f-curved group' refers to a diamine compound in which the nitrogen atom pointing to two amino groups and the combined counter atoms are arranged in a straight line. Specific examples of the linear diamine include p-phenylenediamine and its nuclear-substituted compounds, benzidine and its nuclear-substituted compounds, but they are not particularly limited. These linear diamines may be used singly or in combination of two or more kinds as appropriate. Of these, p-phenylenediamine is particularly preferred. According to this, a polyimide film is excellent in terms of treatment, characteristics, and characteristics. In addition, the so-called "flexible diamine" contains one of the four bent groups such as ether group, methylenyl propyl group, /, fluoro block propyl group, several groups, minus group, and sulfide group in the main chain. An amine, or a case where it does not include a bending group, is a diamine compound having a structure in which a nitrogen atom having 2 amino groups and a carbon atom bonded thereto are not arranged in a straight line. Specific examples of the flexible diamine include 4,4, -oxybisaniline, 1,3-bis (4-aminephenoxy) benzene, n-bis (3-aminephenoxy) benzene, and 4 , 4, -bis (3_aminophenoxy) biphenyl, 4,4, -bis (cardioaminophenoxy) biphenyl, bis (4- (4-aminephenoxy) phenyl) polysulfone, bis (4- (3-Aminophenoxy) phenyl) polyfluorene, 4,4, _diaminediphenylpropane, 4,4, _diaminediphenylmethane, 4,4, -diaminediphenylsulfide, 3,3, diamine diphenyl polyhard, 4,4'-diamine dibenzyl polysulfone, 3,3, _oxodianiline, 3,4, _oxodiphenylamine, 2,4'_oxodi Aniline, 4,4, _diaminediphenyldiethyl and 4,4, _diaminediphenyldisulfide, 4,4, diaminediphenylethyl phosphine, 4,4, -di Amine diphenyl

O:\87\87969-940216.D0C -20- 1243186 N甲基胺、4,4’_二胺二苯基N_苯基胺、13-二胺基苯、n 二胺基苯等,然而其並非特別被限定者。上述彎曲性二胺 只使用1種亦可,適宜地組合2種以上使用亦可。該等之中 尤其使用4,4’_氧雙苯胺較為較佳者。據此,可得與諸物性 之調合出色之聚醯亞胺膜。 上述芳香族二胺中,直線性二胺及彎曲性二胺之使用量 並非特別被限定者,全芳香族二胺成分作為1〇〇 ^^1%之 時,使用直線性二胺於20〜80 m〇l%之範圍内為較佳者,使 用於30〜70mol%之範圍内者更理想,使用於35〜65m〇以 之範圍内者更加理想。 再者,王芳香無一胺成分作為1〇〇 m〇l%之時,彎曲性二 胺於20〜80mol%之範圍内為較佳者,使用於3〇m〇i%〜7〇 mol%之範圍内者更理想,使用於35〜65 m〇i%之範圍内能 之事更加理想。 換句話說,直線性二胺及彎曲性二胺之使用量之上限, 各自為80 mol%以下為較佳者,更較佳為7〇m〇1%以下,更 加較佳為65 mol%以下。再者,下限較佳為2〇 m〇1%以上, 更較佳為30 mol%以上,並且更加較佳為35m〇1%以上。此 外,直線性二胺及彎曲性二胺之使用量使之對比時,全芳 香族二胺成分作為100 m〇l%之時,各自使用2〇〜8〇 m〇l% 之範圍内及80〜2〇111〇1%之範圍内為較佳者,3〇〜7〇111〇1% 之範圍内及70〜30 mol%之範圍内用者更理想,使用35〜65 mol%之範圍内及65〜35 mol%之範圍内者更加理想。 根據直線性二胺之使用量及彎曲性二胺之使用量於上述 O:\87\87969-940216.DOC -21 - 1243186 範圍内’祕模數及線膨關數之調合被保持,改善具軟 式銅箔層疊板或TAB帶之彎曲特性成為容易。 上述直線性二胺及上述彎曲性二胺,其^上述聚酿亞胺 分子(聚ϋ胺酸分子)中之分佈並非特別被限定者,然:而任意 分佈者為較佳者。據此’使高彈性模數及線膨脹係數大: 立成為容易。 ^再者、,於本發明因應對所得之聚醯亞胺膜要求之物性 等,作為上述二胺成分,使用芳香族二胺以外之二胺(其他 之一胺)亦可。其它之二胺之使用量亦非特別被限定者。 (2)關於於本發明之聚醯亞胺膜之製造方法 關於本發明之聚醯亞胺膜之製造方法於以下說明。 上述I醯胺酸之聚合(合成)方法並非特別被限定者,能使 用先Μι習知之方法。於有機溶媒中如同成為大約同莫耳量 (實質性等莫耳之量)一般於有機溶媒中使之溶解酸成分及 一胺成分’使其反應,調製作為聚醯亞胺之前驅體之聚醯 胺酸之有機溶媒溶液(以下稱聚醯胺酸溶液)即可。 使之反應時之條件並非特別被限定者,然而作為反應溫 度-20°C〜90°C之範圍内為較佳者,作為反應時間3〇分〜24 小日守左右之範圍内為較佳者。再者,作為反應時之氣氛, 氬及氮等之不活性氣氛較為較佳者。 上述聚酸胺酸之聚合,使用異於使酸成分及二胺成分反 應之手法之複數種類之聚合方法。具體而言,可適於使用 譬如表示於以下之1)至5)一般之聚合方法。 1)於有機溶媒中溶化芳香族二胺,使該芳香族二胺與與O: \ 87 \ 87969-940216.D0C -20-1243186 N methylamine, 4,4'-diamine diphenyl N-phenylamine, 13-diaminobenzene, n-diaminobenzene, etc., however It is not particularly limited. The bendable diamine may be used alone or in combination of two or more of them. Among these, 4,4'-oxybisaniline is particularly preferred. Accordingly, a polyimide film excellent in blending with various physical properties can be obtained. Among the above-mentioned aromatic diamines, the amount of linear diamine and bendable diamine used is not particularly limited. When the total aromatic diamine component is 100% ^ 1%, the linear diamine is used at 20 to A range of 80 m% is better, a range of 30 to 70 mol% is more preferred, and a range of 35 to 65 m% is more preferred. In addition, when Wang aromatic has no monoamine component as 100 mol%, the flexible diamine is preferably in the range of 20 to 80 mol%, and is used in the range of 30 mol% to 70 mol%. Those within the range are more ideal, and those that can be used within the range of 35 to 65 m% are more ideal. In other words, the upper limit of the amount of linear diamine and bendable diamine used is preferably 80 mol% or less, more preferably 70 mol% or less, and more preferably 65 mol% or less. . Furthermore, the lower limit is preferably at least 20 mol%, more preferably at least 30 mol%, and even more preferably at least 35 mol%. In addition, when the amounts of linear diamine and bendable diamine are compared, when the total aromatic diamine content is 100 ml%, use each within the range of 20 to 80 ml% and 80%. It is better to be in the range of ~ 2,111,01%, more preferably in the range of 30 to 7,101,01%, and 70 to 30 mol%, and the range of 35 to 65 mol% is used. And the range of 65 ~ 35 mol% is more desirable. According to the amount of linear diamine used and the amount of bendable diamine within the above range of O: \ 87 \ 87969-940216.DOC -21-1243186, the blending of the "secret modulus and linear expansion point" is maintained, and the improvement The bending characteristics of the flexible copper foil laminate or TAB tape become easy. The distribution of the linear diamine and the curved diamine is not particularly limited to the polyimide molecules (polyamic acid molecules), but arbitrary distributions are preferred. According to this, the high elastic modulus and the coefficient of linear expansion are large: it becomes easy. ^ In addition, in the present invention, for the physical properties required for the obtained polyimide film, etc., as the diamine component, a diamine other than an aromatic diamine (an other amine) may be used. The amount of other diamines is not particularly limited. (2) Production method of polyimide film of the present invention The production method of polyimide film of the present invention is described below. The method for polymerizing (synthesizing) the amino acid is not particularly limited, and a method known in the art can be used. In an organic solvent, it appears to be approximately the same molar amount (substantially equal to the molar amount). In an organic solvent, the acid component and the monoamine component are dissolved and reacted to prepare a polymer as a precursor of polyimide. An organic solvent solution of phosphonic acid (hereinafter referred to as a polyphosphonic acid solution) is sufficient. The conditions under which the reaction is performed are not particularly limited, but a reaction temperature in the range of -20 ° C to 90 ° C is preferred, and a reaction time in the range of 30 minutes to 24 hours is preferred. By. In addition, as the atmosphere during the reaction, an inert atmosphere such as argon or nitrogen is preferred. For the polymerization of the polyamic acid, a plurality of types of polymerization methods different from the method of reacting the acid component and the diamine component are used. Specifically, general polymerization methods such as those shown in 1) to 5) below can be suitably used. 1) Dissolve the aromatic diamine in an organic solvent, and make the aromatic diamine and

O:\87\87969-940216.DOC -22- !243186 貝同莫耳之芳香族四鲮酸二酐反應聚合之方法。 2) 使方香無四竣酸二野與對該過小莫耳量之芳香族二胺 化σ物^有機溶媒中反應,得到於兩端具酸酐基之預聚物 _ 只之於整個步驟中,芳香族四羧酸二野及芳香族 二胺化合物成為實質上同莫耳一般,使用芳香族二胺化人 物而使之聚合之方法。 " 3) 芳香族四㈣二肝與對該過剩莫耳量之芳香族二胺化 合物於有機溶媒中反應,得於兩端具氨基之預聚合物。續 之,於此追加添加芳香族二胺化合物後,於整個步驟中芳 香私四叛酸二野及芳香族二胺化合物成為實質上同莫耳一 般,使用芳香族四幾酸二野而聚合之方法。 ,)使芳香鉍四羧酸二酐於有機溶媒中溶解及/或分散之 =成為a負上同莫耳—般’使用芳香族二胺化合物使其 5)實貝上同莫耳一般之芳香族四敌酸二肝及芳香族二胺 之混合物於有機溶媒中使其反應而聚合之方法。 使用於上述聚醯胺酸溶液之製作之有機溶媒,即使用於 聚醯胺酸之聚合之聚合用溶媒,若具溶化聚醯胺酸之溶 媒,則其並非特別被限定者。作為具體之一你!,可舉出胺 系溶媒即N,N-二甲基甲醯胺、N,N_:甲基乙醯胺、N_甲基 -2-吨㈣等,其中可使用N,N_:甲基甲酿胺、N,N_二甲^ 乙醯胺較為較佳者。該等有機溶媒,通常單獨使用,然2 因應必要適宜地組合2種以上使用亦可。 再者,關於上述聚醯胺酸溶液之組成並非特別被限定 O:\87\87969-940216.DOC -23- 1243186 者’然而於有機溶媒中聚醯胺酸於5〜35重量%之範圍内被 -化為較佳者’1〇〜30重量%更理想。根據關係範圍内者, 獲得適當之分子量與溶液黏度者成為可能。 上述聚醯亞胺膜’以改善滑動性、熱傳導性、導電性、 抗電軍等之▼之諸特性為目的而添加充填劑亦可。作為充 填劑’並非特別被限定者,然而作為較佳者之具體例,可 舉出二氧化%、氧化鈦、氧魅、氮切、氮㈣、碟酸 氫鈣、磷酸鈣、雲母等。 再者,上述充填劑之粒子直徑’根據重整帶特性及添加 之充填劑之種類變動所得者,其並非特別被限定者,然而 一般平均粒直徑0.05〜100 μπχ之範圍内為較佳者,〇」〜” μπι之範圍内更理想,0el〜50 μιη之範圍内更加理想,〇J〜 25 μιη之範圍内特別理想。若粒子直徑於該範圍内,於聚醯 亞胺膜中容易出現重整質量效果,若不超過該範圍,於聚 醯亞胺膜中可得良好之表面性、機械之特性。 再者’關於上述充填劑之添加份數,亦根據重整帶特性 及充填劑粒子直徑等變動所得者,其並非特別被限定者。 一般充填劑之加添量對聚醯亞胺100重量部於〇〇1〜1〇〇重 量部之範圍内為較佳者,0.01〜90重量部之範圍内更理 想,0.02〜80重量部之範圍内更加理想。若充填劑加添量 不低於該範圍,容易出現充填劑之重整效果,若不超過今 範圍,可保持聚醯亞胺膜良好之機械之特性。 充填劑之加添之方法並非特別被限定者,然而具體上, 譬如可舉出聚合前或聚合中添加於聚合反應液之方法、聚 O:\87\87969-940216.DOC -24- 1243186 醯胺酸之聚合完成後使用3個捲等混煉充填劑之方法、準備 含有充填劑之分散液混合其於聚醯胺酸溶液之方法等。 其中,亦以準備含有充填劑之分散液混合其於聚醯胺酸 溶液之方法,特別是採製膜緊接之前之混合方法為較佳 者。據此,藉由充填劑之製造線之污染能最少。準備含上 述充填劑之分散液時,使用聚醯胺酸之聚合溶媒及同樣之 溶媒為較佳者。再者,《了讓充填劑良好分散,幻吏之分 散狀態穩定化,於對帶物性不帶來影響之範圍内使用份兒 散藥、增加黏性劑等亦可。 於本發明,關於由上述聚醯胺酸溶液製造聚醯亞胺膜之 方法,並非特別被限定者,可使用先前習知之方法。作為 醯亞胺化之方法,可舉出熱醯亞胺化法及化學醯亞胺化 法,然而使用化學醯亞胺化法更理想。據此,可得熱尺寸 穩定性及機械強度出色之聚醯亞胺膜。 其次舉出說明關於本發明之聚醯亞胺膜之製造方法之理 想之一例,但當然本發明之製造方法並非被其所限定。關 於本發明之聚醯亞胺膜之製造方法,a)於有機溶媒中使芳 香族二胺與芳香族四羧酸二酐反應而得聚醯胺酸溶液之步 驟’ b)含上述聚醯胺酸溶液之製膜黏稠劑於支持體上流延 之步驟’ c)上述製膜黏稠劑於支持體上加熱後,由支持體 拆離凝膠膜之步驟,幻更且加熱凝膠膜,醯亞胺化殘存之 醯胺酸’使之乾燥之步驟,至少含其4步驟為較佳者。 於上述製造中,脫水劑亦可併用含醯亞胺化觸媒之硬化 劑為較佳者。 0 :\87\87969-940216.D0C -25- 1243186 取本發明理想之一形態為例,藉由併用硬化劑之化學酿 亞胺化之聚醯亞胺膜之製造步驟來說明。 化學醯亞胺化法,對聚醯胺酸溶液,以任一代表無水醋 酸等之酸酐之脫水劑及代表異喹啉、β_甲基峨σ定、< σ定等 之第3級胺類等之醯亞胺化觸媒,使其作用之方法。 化學醯亞胺化法併用熱醯亞胺化法亦可。加熱條件可根 據聚醯胺酸之種類、膜厚等變動得之。 a) 於有機溶媒中使芳香族二胺與芳香族四缓酸二野反應 以得聚醯胺酸溶液, b) 脫水劑及醯亞胺化觸媒於聚醯胺酸溶液中以低溫混合 之製膜黏稠劑,於玻璃板、鋁箔、環狀不銹鋼帶、不錢鋼 滾筒等之支持體上鑄造膜狀, C)於支持體上以80。(:〜200°c、較佳為l〇(TC〜i8(rc之溫 度加熱’根據活化脫水劑及酿亞胺化觸媒之硬化及/或乾燥 之後’由支持體拆離而得聚隨胺酸膜(以下稱凝膠膜)。 凝膠膜係從聚隨胺酸向聚醯亞胺之硬化之中間階段,呈 自我支持性,式1 (A-B)xl〇〇/B···式 1 式1中,A、B係表示以下者。 A :凝膠膜之重量 B:由凝膠膜以450°C20分鐘加熱後之重量 所算出之揮發含量為5〜500〇/〇之範圍,較佳為5〜1〇〇%,更 較佳為10〜80%,最較佳為3〇〜60%之範圍。 使用該範圍之膜為適宜,一旦偏差具引起機械之強度之 O:\87\87969-940216.DOC -26- 1243186 降低等。 d)固定上述凝膠膜端部,迴避硬化時之收縮乾燥,並且 去除水殘餘溶媒、加添劑及觸媒,殘留之醯胺酸完全醯亞 胺化,可得本發明之聚醯亞胺膜。 此時,最終以400〜58(TC之溫度加熱5〜4〇〇秒鐘為較佳 者。若較該溫度高及/或時間長,衍生膜之熱劣化產生問 題。相反若較該溫度低及/或時間短則無法出現預定之效 果。 所得之聚醯亞胺膜之厚度並未特別被限定,然而特別使 用作為TAB帶及FPC之基膜時,帶之厚度為1〇-125 之範 圍内為較佳者,2(Μ〇〇μιη之範圍内更理想,25_9〇_之範 圍内更加理想,40-80 μπι之範圍内特別理想。 如此可得,關於本發明之聚醯亞胺膜,如前述一般,從 loot:至20(TC之平均線膨脹係數為18〜28 ppmrc之範圍 内,滿足彈性模數為4.5GPa以上,吸濕膨脹係數為i3ppm 以下之條件。 (3)本發明之用途(本發明之有用性) 關於本發明之聚醯亞胺膜,可使用因應其物性之各式各 樣之用途,特別可適於使用用於FPC、TAB帶等之FC(膜載 助·)關於本發明之FC帶,設置黏著劑層於有關本發明之聚 酏亞胺膜上,於黏著劑層上設置保護層作為3層結構之所謂 f作為黏著劑層之材f,譬如可舉出環氧系樹月旨、尼龍 夂丨生袞氧系树脂、丙烯系樹脂、聚醯亞胺系樹脂、石炭酸 系树月曰石炭酸變性環氧系樹脂、聚醯胺醯亞胺系樹脂等,O: \ 87 \ 87969-940216.DOC -22-! 243186 A method for the reaction polymerization of Moore's aromatic tetrakistic dianhydride. 2) The Fangxiang Wuquan acid second field is reacted with the aromatic diamine sigma ^ organic solvent with an excessively small molar amount to obtain a prepolymer having acid anhydride groups at both ends _ only in the entire step Aromatic tetracarboxylic diamino and aromatic diamine compounds become substantially the same as Mol, and a method of polymerizing them using an aromatic diamine is used. " 3) Aromatic tetramethylene di liver reacts with the excess molar amount of the aromatic diamine compound in an organic solvent to obtain a prepolymer having amino groups at both ends. Continuing, after the aromatic diamine compound is added here, the aromatic tetraamine diamino compound and the aromatic diamine compound become substantially the same as Moore in the entire step, and the aromatic tetrakidic acid difield is used for polymerization. method. ,) Make aromatic bismuth tetracarboxylic dianhydride dissolve and / or disperse in organic solvent = become a minus the same as Moore-using 'aromatic diamine compounds to make it 5) the same as Moore's aromatic A method of polymerizing a mixture of diene tetradicarboxylic acid and aromatic diamine in an organic solvent. The organic solvent used for the production of the polyamic acid solution is not particularly limited even if it has a solvent for dissolving the polyamic acid, even if it is a polymerization solvent used for the polymerization of the polyamic acid. As a specific one you! Examples include N, N-dimethylformamide, N, N_: methylacetamide, N_methyl-2-tonamidine, and the like, among which amine-based solvents are N, N_: methylformamide Sterile amine and N, N-dimethyl ^ acetamide are preferred. These organic solvents are usually used alone, but two or more of them may be used in combination as appropriate. In addition, the composition of the above-mentioned polyamic acid solution is not particularly limited. O: \ 87 \ 87969-940216.DOC -23-1243186 Anyone, however, the polyamic acid is in the range of 5 to 35% by weight in the organic solvent. It is more preferable to be reduced to '10 to 30% by weight. It is possible to obtain an appropriate molecular weight and solution viscosity according to the relationship. The polyimide film 'may be added with a filler for the purpose of improving various properties such as sliding properties, thermal conductivity, electrical conductivity, and resistance to electric power. The filler 'is not particularly limited, but specific examples of preferred ones include% dioxide, titanium oxide, oxygen charm, nitrogen cutting, nitrogen oxide, calcium dihydrogenate, calcium phosphate, mica, and the like. In addition, the particle diameter of the filler mentioned above is obtained according to the characteristics of the reforming belt and the type of filler added, which is not particularly limited, but generally the average particle diameter is in the range of 0.05 to 100 μπχ. 〇 ″ ~ ”μπ is more desirable, 0el ~ 50 μιη is more desirable, and 〇J ~ 25 μιη is particularly desirable. If the particle diameter is within this range, weight is likely to appear in the polyimide film. If the mass effect does not exceed this range, good surface properties and mechanical properties can be obtained in the polyimide film. In addition, the amount of the filler added above is also based on the characteristics of the reforming belt and the filler particles. Those with changes in diameter are not particularly limited. The addition amount of the general filler is preferably within the range of 0.001 to 100 parts by weight based on 100 parts by weight of polyimide, 0.01 to 90 parts by weight. It is more ideal within the range of 0.02 to 80 parts by weight. If the amount of filler added is not less than this range, the reforming effect of the filler is likely to occur. If it does not exceed this range, Polyurethane can be maintained amine Good mechanical properties. The method of adding filler is not particularly limited, but specifically, for example, the method of adding to the polymerization reaction solution before or during polymerization, poly O: \ 87 \ 87969-940216. DOC -24-1243186 A method of kneading a filler using 3 rolls after the completion of polymerization of amidine, a method of preparing a dispersion containing a filler and mixing it in a polyamic acid solution, etc. Among them, a preparation containing a filler is also prepared. The method of mixing the dispersant of the agent in the polyamic acid solution, especially the method immediately before the production of the film is preferred. According to this, the pollution energy of the manufacturing line through the filler is the least. Prepare the filler When dispersing liquid, it is better to use polyamic acid polymerization solvent and the same solvent. Furthermore, "The dispersion of fillers is well dispersed, and the dispersion state of the magicians is stabilized, which does not affect the physical properties of the tape. It is also possible to use fener powder, viscosity-increasing agent, etc. in the scope. In the present invention, the method for producing a polyimide film from the polyamic acid solution is not particularly limited, and a conventionally known method can be used. As Examples of the method of fluoridation include thermal fluoridation and chemical fluoridation. However, it is more preferable to use chemical fluoridation. Based on this, a polymer having excellent thermal dimensional stability and mechanical strength can be obtained.醯 imine film. Next, an ideal example for explaining the method for producing a polyimide film of the present invention will be described, but of course, the method of producing the present invention is not limited thereto. About the production of a polyimide film of the present invention Method, a) the step of reacting an aromatic diamine with an aromatic tetracarboxylic dianhydride in an organic solvent to obtain a polyamic acid solution 'b) a film-forming viscose containing the above polyamino acid solution is flowed on a support Step 'c) After the above film-forming viscose is heated on the support, the step of detaching the gel film from the support, changing the gel film and heating the gel film, and drying the remaining imine acid to dry it The step, including at least 4 steps thereof, is the better one. In the above-mentioned production, a dehydrating agent may also be used in combination with a curing agent containing a sulfonium imidization catalyst. 0: \ 87 \ 87969-940216.D0C -25-1243186 Take one of the ideal forms of the present invention as an example, and explain it by the manufacturing steps of chemically brewed polyimide film using a hardener. Chemical ammonium imidization method, for polyacrylic acid solution, any dehydrating agent representing anhydride of anhydrous acetic acid, etc., and tertiary amines representing isoquinoline, β-methyl eσdine, < σdine etc. A similar method of imidization catalyst to make it work. The chemical amidine method may be used in combination with the thermal amidine method. The heating conditions can be changed according to the type and film thickness of the polyamic acid. a) The aromatic diamine is reacted with the aromatic tetrahydroacid di-field in an organic solvent to obtain a polyamic acid solution. b) The dehydrating agent and the ammonium imidization catalyst are mixed in the polyamino acid solution at low temperature. Film-forming viscose is cast into a film on a support such as glass plate, aluminum foil, ring-shaped stainless steel strip, stainless steel roller, etc. C) 80 on the support. (: ~ 200 ° C, preferably 10 (TC ~ i8 (rc temperature heating 'according to the hardening and / or drying of the activated dehydrating agent and the imidization catalyst' after being detached from the support to obtain the polymer Amino acid film (hereinafter referred to as gel film). The gel film is a self-supporting intermediate stage from the curing of polyacrylic acid to polyimide, with the formula 1 (AB) x100 / B ···· 1 In formula 1, A and B represent the following: A: the weight of the gel film B: the volatile content calculated from the weight of the gel film after heating at 450 ° C for 20 minutes is in the range of 5 to 500/0, It is preferably 5 to 100%, more preferably 10 to 80%, and most preferably 30 to 60%. The use of a film in this range is suitable, and once the deviation has a mechanical strength of O: \ 87 \ 87969-940216.DOC -26- 1243186 lowered, etc. d) Fix the end of the gel film to avoid shrinkage and drying during hardening, and remove the residual solvent, additives and catalysts in the water, and the residual ammonium acid is completely The polyimide film of the present invention can be obtained by amidine imidization. At this time, it is better to finally heat at a temperature of 400 to 58 ° C. for 5 to 400 seconds. If it is higher than this temperature and / or time long, The thermal degradation of the green film causes problems. On the contrary, if the temperature is lower than the temperature and / or the time is short, the predetermined effect cannot be achieved. The thickness of the obtained polyimide film is not particularly limited, but it is especially used as a TAB tape and FPC. In the case of a base film, the thickness of the belt is preferably in the range of 10-125, more preferably in the range of 2 μm, more preferably in the range of 25-90, and particularly desirable in the range of 40-80 μm. In this way, as for the polyimide film of the present invention, as described above, the average linear expansion coefficient of loot: 20 to 20 (TC is 18 to 28 ppmrc), and the elastic modulus is 4.5 GPa or more. The condition for the wet expansion coefficient to be i3 ppm or less. (3) Applications of the present invention (usefulness of the present invention) The polyimide film of the present invention can be used in various applications depending on its physical properties, and is particularly suitable for Use of FC (Film Loading Assistance) for FPC, TAB tape, etc. Regarding the FC tape of the present invention, an adhesive layer is provided on the polyimide film of the present invention, and a protective layer is provided on the adhesive layer as three layers. The so-called f of the structure is used as the material f of the adhesive layer. Epoxy purpose tree months, nylon Pangshu green gun-based resins, acrylic resin, polyimide resin, carbolic acid-based tree May said carbolic acid modified epoxy resin, polyamide-imide-based resin,

O:\87\87969-940216.DOC -27- 1243186 然而並非特別被限定於該等。再者,僅管作為保護層之材 質,譬如可舉出PET、EVA等,然而並非特別被限定於該等。 再者,關於本發明之FPC及TAB帶,關於本發明之聚醯亞 胺膜之至少於一面,若介/或不介黏著劑層形成金屬導電 層八並非特別被限定者。換句話說,關於本發明之Fpc 及TAB页中,至少具由上述聚醯亞胺膜組成之層及金屬導 電層間之黏著劑之構成即佳。#纟,即使僅於由聚酿亞胺 膜組成之層(基膜)之片面層疊金屬導電層亦佳,而於金屬導 電層兩面層疊亦佳。 因此,於本發明’包含由聚醯亞胺膜/金屬導電層組成之 2層結構之層疊體;由金屬導電層/聚醒亞胺膜/金屬導電層 組成之3層結構之層疊體;由聚醯亞胺膜/黏著劑層/金屬導 電“成之3層結構之層登體;由金屬導電層/黏著劑層/聚 醯亞胺膜/黏著劑層/金屬導電層組成之5層結構之層疊體 作為上述黏著劑層之材質,譬如可舉出環氧系樹脂、八 4,眭%氧系树脂、丙烯系樹脂、聚醯亞胺系樹脂、石力 :系樹月日;δ厌g㈣性環氧系樹脂、㈣胺醯亞胺系樹用 等’但並非特別被限定於該等。此外作為用於上述金屬導 電層之金屬’譬如可舉出銅等,但並非特別被限定於該等, =’使用關於本發明之聚醢亞胺膜,藉黏著劑黏合趣 冶、FPC及TAB帶時,使點著劑完全硬化且於m 濕度60%環垮下1 〇n h* ^、 小^周濕後之彎曲量,將黏著面作 侧之料作為加,”面w㈣料為減=O: \ 87 \ 87969-940216.DOC -27-1243186 However, it is not limited to these. Furthermore, the materials used as the protective layer include, for example, PET and EVA, but they are not particularly limited to these. Furthermore, regarding the FPC and TAB tapes of the present invention, and on at least one side of the polyimide film of the present invention, it is not particularly limited if the metal conductive layer is formed with or without the adhesive layer. In other words, in the Fpc and TAB pages of the present invention, it is preferable to have at least a constitution of an adhesive between a layer composed of the above polyimide film and a metal conductive layer. # 纟 Even if the metal conductive layer is laminated only on one side of the layer (base film) composed of the polyimide film, it is also preferable to laminate on both sides of the metal conductive layer. Therefore, in the present invention, a laminate including a two-layer structure composed of a polyimide film / metal conductive layer; a laminate having a three-layer structure composed of a metal conductive layer / polyimide film / metal conductive layer; Polyimide film / adhesive layer / metal conductive layered structure; 3-layer structure consisting of metal conductive layer / adhesive layer / polyimide film / adhesive layer / metal conductive layer The laminated body is used as the material of the adhesive layer. For example, epoxy-based resin, 8.4% oxygen-based resin, propylene-based resin, polyimide-based resin, and stone force: the tree moon and the sun; "Ethylene-based epoxy resins, amines, and imine-based trees" are not particularly limited to these. Examples of the metal used for the metal conductive layer include copper, but are not particularly limited to these. These, = 'Using the polyimide film of the present invention, when bonding Quye, FPC, and TAB tapes with an adhesive, the spotting agent is completely hardened and collapsed at 60% humidity in 100% * ^, For the small amount of bending after cyclic wetness, add the adhesive surface as the side material, and the "surface w material is reduced =

O:\87\87969-940216.DOC -28- 1243186 如下。銅不做餘刻法之狀態,彎曲量較佳為〇5 mm以下, 並且更較佳為Omm以下,特別較佳為_〇·5 mm以下。再者, 藉由蝕刻法完全除去銅箔之狀態,彎曲量較佳為3〇 mm以 下,並且更較佳為2.5 mm以下,特別較佳為2·0 mm以下。 藉由姓刻法完全除去鋼箔及附著銅箔之狀態之彎曲量,若 同%滿足該等範圍之時,可消除加工、封裝步驟之彎曲而 來之不適點。 (4)具體之實施例 以下,基於實施例及比較例更具體地說明本發明,本發 明亚非被限定於該等。再者,以實施例或比較例所得到之 聚醯亞胺膜之彈性模數之測量係以ASTM D882為準則來進 行再者所得之聚酸亞胺膜之線膨脹係數、吸濕膨脹係 數係如次下一般測量。 〔線膨脹係數之測量〕 從100°c至200°C之平均線膨脹係數之測量,使用精工電 子(股)公司製TMA120C來進行。樣品尺寸作為幅度3 _、 長度10 mm。載上3g之負荷,以1〇。〇/11^11至1〇t>c 〜4〇〇〇c 一 旦升溫之後,冷卻至10。〇。更使之以1〇t:/min升溫,以於 第2次之升溫時之1〇〇。(:及2〇〇1之熱膨脹率作為平均值來 算出。 〔吸濕膨脹係數之測量〕 測量之膜24小時放置於5(rc、相對濕度3〇%之環境測驗 機’測定之膜尺寸(L1)。其次其膜24小時放置於⑽、相 對濕度80%之環境測驗機,測定之膜尺寸(L2),根據下列公 O:\87\87969-940216.DOC -29- 1243186 式算出其吸濕膨脹係數。 及濕私脹係數(ppm)= (L1_L2)+L 1+(80-30)χ106 再者,從所得之聚醯亞胺膜,如下一般製作TAB帶,測 量彎曲。 〔TAB帶之作成〕 於此合聚醯胺樹脂(日本利氯產公司製黏結料M1276) 5〇 重里部、雙石炭酸A型環氧樹脂對混合(油化殼牌環氧樹脂 公司製Eplcoat828) 30重量部 '甲酚醛清漆型環氧樹脂1〇重 里邛、甲苯/異丙醇1/1混合溶液15〇重量部之溶液,調製混 合重置部二胺二苯基聚砜/雙氰胺4/1 2〇%乙二醇甲醚溶液 4 5之黏著劑溶液。 於厚度25 μιη之PET膜上如同乾燥後成為u μηι 一般塗 布以12〇 C 2分鐘乾燥上述黏著劑。所得之Β階段黏著劑附 著PET膜分隔寬度26 mm ° 上述之B(^丨又黏著劑附著pet膜與幅度35 mm之聚酿亞胺 膜中央部黏合,以90°C、1 kg/cm2之壓力壓著。拆離pET膜, 銅箱(三井金屬製,厚度VLP18 μιη)用卷黏合法與拆離pET 膜之聚醯亞胺膜之表面黏合(無蝕刻法ΤΑβ帶)。黏合之溫度 為120 C、壓力為2 kg/cm2量。 上述銅黏合成品以5 0 C 3小時、3 0 °C 3小時、12 0。〇 3小時、 14(TC3小時、160°C4小時之階段加熱後徐冷卻,進行黏著 劑之硬化。將所得之帶作為「銅附著帶」。 黏著劑之硬化後,根據蝕刻法完全除去銅箱。將所得之 ▼作為「銅全姓刻法」。 O:\87\87969-940216.DOC -30- 1243186 〔彎曲量之測量〕 彎曲量之值係上述之順序製作之TAB帶切為長度40 mm X幅度35 mm方形來測量。試驗片於相對濕度60%、溫度23 °C之房間放置72,之後於平面上靜置,測量四角浮起之高 度。彎曲量之值,以4件數據之平均值表示。 【實施例1】 於N,N-二甲基甲醯胺(DMF) 407.5 g溶解4,4’-氧雙苯胺 (ODA) 21.98 g及對苯二胺溶化(PDA) 7.91 g,保持該溶液於 0°C。於此,徐徐地添加3,3’,4,4L二苯甲酮四羧酸二酐(BTDA) 29.47 g,攪拌1小時,使BTDA完全溶化。於該溶液徐徐地 添加對伸苯基雙(偏苯三酸單酯酐)(TMHQ) 25.15 g,攪拌1 小時後,再添加焦苯六甲酸二酐(PMDA) 7.98 g,攪拌1小 時,得到於23°C中之溶液黏度3000泊、固形分濃度18.5 wt% 之聚醯胺酸溶液。再者,此時添加之單體成分mol%顯示於 表1。再者,於表1及後述之表3中,單體組成係依添加單體 之順序,從最上階段往下階段記載。 於該聚醯胺酸溶液100 g混合攪拌包含無水醋酸11.4 g, 異奎林4.8 g及DMF 33.8 g之硬化劑。所得之溶液藉由離心 分離脫氣後,澆鑄塗敷於鋁箔上。從攪拌至脫氣係同時冷 卻至〇°C同時進行。於90°C,600秒加熱所得之鋁箔及聚醯 胺酸溶液之層疊體,以獲得含自我支持性之凝膠帶。從鋁 箔拆離該凝膠帶,固定於框架。於120°C、250°C、350°C、 450°C,各180秒加熱該凝膠帶後,再於400°C之遠紅外線烤 爐1 80秒加熱處理。使用該做法所得之厚度50 μιη之聚醯亞 O:\87\87969-940216.DOC -31 - 1243186 胺膜,依上述方法製作TAB帶。 針對「附銅帶」及「銅全蝕刻帶」測量所得之聚醯亞胺 膜之彈性模數、平均線膨脹係數、吸濕膨脹係數及TAB帶 之彎曲量。測量結果顯示於表2。 【實施例2】 於〇]^卩407.5 8溶化00八17.9〇8及?0八9.678,保持該溶 液於0°C。於此,徐徐地添加BTDA 28.81 g,攪拌1小時, 使BTDA完全溶化。於該溶液徐徐地添加TMHQ 24.59 g,攪 拌1小時後,再添加BTDA 11.52 g攪拌1小時,獲得於23°C 中之溶液黏度2800泊、固形分濃度18.5 wt%之聚醯胺酸溶 液。再者,此時添加之單體成分mol%顯示於表1。再者, 於表1中BTDA之mol%為50及20,其係表示於最初添加之 BPDA及之後添加之BPDA之量。 使用該聚醯胺酸溶液以外,與實施例1同樣做法而獲得厚 度50 μιη之聚醯亞胺膜及TAB帶。聚醯亞胺膜及TAB帶之特 性顯示於表2。 【實施例3】 於 DMF 407.5g 溶化 ODA 17.90 g 及 PDA 9.67 g,保持該溶 液於0°C。於此,徐徐地添加BTDA 3 8.61 g,攪拌1小時, 使BTDA完全溶化。於該溶液徐徐地添加TMHQ 24.59 g,攪 拌1小時後,再添加BTDA 1.73 g,攪拌1小時,獲得於23°C 中之溶液黏度3 10000泊、固形分濃度18.5 wt%之聚醯胺酸 溶液。再者,此時添加之單體成分mol%顯示於表1。再者, 於表1中BTDA之mol%為50及20,其係表示於最初添加之 O:\87\87969-9402t6.DOC -32- 1243186 BPDA及之後添加之BPDA之量。 使用該聚醯胺酸溶液以外,與實施例1同樣做法而獲得厚 度50 μιη之聚醯亞胺膜及TAB帶。聚醯亞胺膜及TAB帶之特 性顯示於表2。 【實施例4】 於 DMF 407.5 g溶化 ODA 19.86 g、PDA 8.77 g,保持該溶 液於0°C。於此,徐徐地添加BTDA 29.04 g,攪拌1小時, 使BTDA完全溶化。於該溶液徐徐地添加TMHQ 28.92 g,攪 拌1小時後,再添加PMDA 5.90 g,攪拌1小時,獲得於23°C 中之溶液黏度2900泊、固形分濃度18.5 wt%之聚醯胺酸溶 液。再者,此時添加之單體成分mol%顯示於表1。 使用該聚醯胺酸溶液以外,與實施例1同樣做法而獲得厚 度50 μιη之聚醯亞胺膜及TAB帶。聚醯亞胺膜及TAB帶之特 性顯示於表2。 【實施例5】 於 DMF 407.5 g 溶化 ODA 18.66 g、PDA 10.07 g,保持該 溶液於0°C。於此,徐徐地添加BTDA 3 0.02 g,攪拌1小時, 使BTDA完全溶化。於該溶液徐徐地添加TMHQ 25.62 g,攪 拌1小時後,再添加PMDA 8.13 g,攪拌1小時,獲得於23°C 中之溶液黏度3200泊、固形分濃度18.5 wt%之聚醯胺酸溶 液。再者,此時添加之單體成分mol%顯示於表1。 使用該聚醯胺酸溶液以外,與實施例1同樣做法獲得厚度 50 μιη之聚醯亞胺膜及TAB帶。聚醯亞胺膜及TAB帶之特性 顯示於表2。 O:\87\87969-940216.DOC -33- 1243186 【實施例6】 於 DMF 407.5 g 溶化 ODA 22.92 g、PDA8.25 g,保持該溶 液於0°C。於此,徐徐地添加BTDA 18.44g,攪拌1小時,使 BTDA完全溶化。於該溶液徐徐地添加TMHQ 26.23 g,攪拌 1小時後,再添加PMDA 16.65 g,攪拌1小時,獲得於23°C 中之溶液黏度3000泊、固形分濃度18.5 wt%之聚醯胺酸溶 液。再者,此時添加之單體成分mo 1°/。顯示於表1。 使用該聚醯胺酸溶液以外,與實施例1同樣做法獲得厚度 50 μιη之聚醯亞胺膜及TAB帶。聚醯亞胺膜及TAB帶之特性 顯示於表2。 【實施例7】 於 DMF 407.5 g 溶化 ODA25.13 g、PDA7.31 g,保持該溶液 於〇°C。於此,徐徐地添加BTDA 12.44 g,攪拌1小時,使 BTDA完全溶化。於該溶液徐徐地添加TMHQ 26.55 g,攪拌1 小時後,再添加PMDA 21.06 g,攪拌1小時,獲得於23^:中 之溶液黏度3000泊、固形分濃度18.5 wt%之聚醯胺酸溶 液。再者,此時添加之單體成分mol%顯示於表1。 使用該聚醯胺酸溶液以外,與實施例1同樣做法而獲得厚 度50 μιη之聚醯亞胺膜及TAB帶。聚醯亞胺膜及TAB帶之特 性顯示於表2。 【實施例8】 於 DMF 407.5 g溶化 ODA 18.86 g、PDA 10.19 g,保持該溶 液於0°C。於此,徐徐地添加3,3f,4,4’-聯苯四羧酸二酐(BPDA) 11.09 g,攪拌1小時,使BPDA完全溶化。於該溶液徐徐地 O:\87\87969-940216.DOC -34- 1243186 添加BTDA 18.22 g,攪拌1小時後,添加TMHQ 25.91 g,攪拌 1小時,再添加PMDA 8.22 g,獲得於23°C中之溶液黏度2700 泊、固形分濃度18.5 wt%之聚醯胺酸溶液。再者,此時添 加之單體成分mol%顯示於表1。 使用該聚醯胺酸溶液以外,與實施例1同樣做法而獲得厚 度50 μιη之聚醯亞胺膜及TAB帶。聚醯亞胺膜及TAB帶之特 性顯示於表2。 【比較例1】 於 DMF 407.5 g 溶化 ODA 21.48 g、PDA 11.06 g,保持該 溶液於0°C。於此,徐徐地添加BPDA 31.56 g,攪拌2小時, 使BPDA完全溶化。於該溶液徐徐地添加PMDA 14.04 g,攪 拌1小時後,再添加BTDA13.83g,攪拌1小時,獲得於23°C 中之溶液黏度2800泊、固形分濃度18.5 wt%之聚醯胺酸溶 液。再者,此時添加之單體成分mol%顯示於表3。 使用該聚醯胺酸溶液以外,與實施例1同樣做法而獲得厚 度50 μιη之聚醯亞胺膜及TAB帶。聚醯亞胺膜及TAB帶之特 性顯示於表4。 【比較例2】 於 DMF 407.5 g 溶化 ODA 19.20 g、PDA 10.37 g,保持該 溶液於0°C。於此,徐徐地添加BPDA 28.21 g,如,攪拌2 小時,使BPDA完全溶化。於該溶液徐徐地添加TMHQ 26.3 6 g,攪拌1小時後,再添加PMDA 8.36 g,攪拌1小時,得於 23°C之溶液黏度2800泊、固形分濃度18.5 wt%之聚醯胺酸 溶液。再者,此時添加之單體成分mol%之顯示於表3。 Ο :\87\87969-940216. DOC -35- 1243186 使用該聚醯胺酸溶液以外,與實施例1同樣做法而獲得厚 度50 μπι之聚醯亞胺膜及TAB帶。聚醯亞胺膜及TAB帶之特 性顯示於表4。 【比較例3】 於DMF 407.5 g溶化ODA 19.92 g,保持該溶液於0°C。於 此,徐徐地添加PMDA 16.49 g,攪拌1小時,使PMDA完全 溶化。於該溶液使PDA 10.76 g溶化後,徐徐地添加17.57 g 之BPDA,攪拌2小時,使BPDA完全溶化。更且,徐徐地添 加TMHQ 26.45 g,攪拌1小時,再添加PMDA 1·30 g,攪拌1 小時,獲得於23°C中之溶液黏度3 100泊、固形分濃度18.5 wt%之聚醯胺酸溶液。再者,此時添加之單體成分mol%顯 示於表3。並且,於表3中PMDA之mol%為50及20,其係表 示於最初添加之PMDA及之後添加之BPDA之量。 使用該聚醯胺酸溶液以外,與實施例1同樣做法而獲得厚 度50 μπι之聚醯亞胺膜及TAB帶。聚醯亞胺膜及TAB帶之特 性顯示於表4。 【比較例4】 於 DMF 407.5 g溶化 ODA3 0.21 g、PDA5.15 g,保持該溶 液於0°C。於此,徐徐地添加TMHQ 26.39 g,攪拌1小時後, 再添加PMDA 3 0.75 g,攪拌1小時,獲得於23°C中之溶液黏 度2900泊、固形分濃度18.5 wt%之聚醯胺酸溶液。再者, 此時添加之單體成分mol%顯示於表3。 使用該聚醯胺酸溶液以外,與實施例1同樣做法而獲得厚 度50 μιη之聚醯亞胺膜及TAB帶。聚醯亞胺膜及TAB帶之特 O:\87\87969-940216.DOC -36- 1243186 性顯示於表4。 【比較例5】 於DMF 407.5 g溶化ODA 44.27 g,保持該溶液於0°C。於 此,徐徐地添加PMDA 48.23 g,攪拌2小時,使PMDA完全 溶化,獲得於23°C之溶液中黏度2800泊、固形分濃度18.5 wt%之聚醯胺酸溶液。再者,此時添加之單體成分mol%顯 示於表3。 使用該聚醯胺酸溶液以外,與實施例1同樣做法而獲得厚 度50 μιη之聚醯亞胺膜及TAB帶。聚醯亞胺膜及TAB帶之特 性顯示於表4。 【比較例6】 於 DMF 407.5 g 溶化 ODA 24.87 g、PDA 13.43 g,保持該 溶液於0°C。於此,徐徐地添加PMDA 54.19 g,攪拌2小時, 使PMDA完全溶化,獲得於231中之溶液黏度2900泊、固形 分濃度1 8.5 wt%之聚醯胺酸溶液。再者,此時添加之單體 成分mol%顯示於表3。 使用該聚醯胺酸溶液以外,與實施例1同樣做法而獲得厚 度50 μιη之聚醯亞胺膜及TAB帶。聚醯亞胺膜及TAB帶之特 性顯示於表4。 【比較例7】 於 DMF 489 g溶化 ODA 26.19 g、PDA 14.14 g,保持該溶 液於0°C。於此,徐徐地添加BTDA42.14 g,攪拌1小時後, 再徐徐地添加PMDA 28.53 g,攪拌2小時,使PMDA完全溶 化,獲得於23 °C中之溶液黏度3000泊、固形分濃度18.5 wt% Ο :\87\87969-940216.DOC -37- 1243186 之聚醯胺酸溶液。再者,此時添加之單體成分mol%顯示於 表3。 使用該聚醯胺酸溶液以外,與實施例1同樣做法而獲得厚 度50 μιη之聚醯亞胺膜及TAB帶。聚醯亞胺膜及TAB帶之特 性顯示於表4。 【比較例8】 揭示於上述曰本國公開專利公報「特開平9-235373」,作 為酸成分使用3,3’,4,4’-二苯曱酮四羧酸二酐之與實施例11 同樣之單體組成而獲得聚醯胺酸。各單體之添加重量係 PPD 5.93 g、PMDA 11.64 g、ODA 3 2.97 g、BTDA 17.68 g、 PMDA 24.28 g 〇 使用該聚醯胺酸溶液以外,與實施例1同樣做法而獲得厚 度5 0 μιη之聚醯亞胺膜,測量吸濕膨脹係數時,其為1 8 ppm,成為非常大之數值。由此,以上述公報表示之技術, 未實現使吸濕膨脹係數變小之事。 O:\87\87969-940216.DOC 38- 1243186 [表1 ] 實施例 單體組成(mol%) ODA PDA TMHQ BTDA PMDA BPDA 1 60 40 30 50 20 2 50 50 30 50 20 3 50 50 30 67 3 4 55 45 35 50 15 5 50 50 30 50 20 6 60 40 30 30 40 7 65 35 30 20 50 8 60 50 30 30 20 20 O:\87\87969-940216.DOC -39- 1243186O: \ 87 \ 87969-940216.DOC -28-1243186 is as follows. In the state where copper is not subjected to the engraving method, the bending amount is preferably 0.5 mm or less, more preferably 0 mm or less, and particularly preferably _0.5 mm or less. In addition, in a state where the copper foil is completely removed by an etching method, the bending amount is preferably 30 mm or less, more preferably 2.5 mm or less, and particularly preferably 2.0 mm or less. The bending amount in the state of the steel foil and the copper foil attached is completely removed by the last name engraving method. If the same percentages satisfy these ranges, the discomfort caused by the bending of the processing and packaging steps can be eliminated. (4) Specific examples Hereinafter, the present invention will be described more specifically based on examples and comparative examples. The present invention is not limited to these. Moreover, the measurement of the elastic modulus of the polyimide film obtained in the examples or comparative examples is based on ASTM D882. The linear expansion coefficient and the hygroscopic expansion coefficient of the polyimide film obtained are based on ASTM D882. The next general measurement. [Measurement of linear expansion coefficient] Measurement of the average linear expansion coefficient from 100 ° C to 200 ° C was performed using TMA120C manufactured by Seiko Instruments Inc. The sample size is taken as a width of 3 mm and a length of 10 mm. Load a 3g load to 10%. 〇 / 11 ^ 11 to 10t > c to 40,000c Once the temperature rises, it is cooled to 10 ° C. 〇. Furthermore, the temperature was raised at 10 t: / min, so as to be 100 at the second temperature increase. (: And the thermal expansion coefficient of 2001 are calculated as the average value. [Measurement of the hygroscopic expansion coefficient] The measured film is left for 24 hours at 5 (rc, relative humidity of 30% in an environmental testing machine to measure the film size ( L1). Secondly, the film is placed in an environmental testing machine with a relative humidity of 80% for 24 hours. The measured film size (L2) is calculated by the following formula: O: \ 87 \ 87969-940216.DOC -29-1243186 Coefficient of wet expansion and coefficient of wet expansion (ppm) = (L1_L2) + L 1+ (80-30) χ106 Furthermore, from the obtained polyimide film, a TAB tape is generally produced as follows, and the bending is measured. [TAB tape Production] Here, polyamidoamine resin (bonding material M1276, manufactured by Nippon Lekko Corporation) was mixed with 50 weight parts, and bis-carbonic acid A-type epoxy resin was mixed (Eplcoat828, manufactured by Petrochemical Shell Epoxy Co., Ltd.) 30 parts by weight. Cresol novolac epoxy resin 10 weight percent, toluene / isopropanol 1/1 mixed solution 15 weight parts of the solution, to prepare the mixed reset part diamine diphenyl polysulfone / dicyandiamide 4/1 2 % Glycol Methyl Ether Solution 4 5 Adhesive solution. On a 25 μm thick PET film, it looks like u μηι after drying. The cloth was dried at 120 ° C for 2 minutes. The obtained B-stage adhesive was attached to the PET film and separated by a width of 26 mm. The above B (^ 丨 adhesive was attached to the pet film and the center of the polyimide film with a width of 35 mm. Adhesion, pressing at 90 ° C, 1 kg / cm2 pressure. Detach pET film, copper box (Mitsui metal, thickness VLP18 μm) with a roll adhesion method and the surface of the polyimide film of the pET film (Taf β tape without etching method). The bonding temperature is 120 C, and the pressure is 2 kg / cm2. The above copper-bonded composite product is 50 C for 3 hours, 30 ° C for 3 hours, 12 0.03 hours, 14 ( After heating at TC for 3 hours and 160 ° C for 4 hours, it is slowly cooled to harden the adhesive. The resulting tape is referred to as a "copper adhesive tape". After the adhesive is hardened, the copper box is completely removed according to the etching method. The resulting ▼ is used as "Bronze full surname carving method." O: \ 87 \ 87969-940216.DOC -30- 1243186 [Measurement of Bending Amount] The value of the bending amount is a TAB tape made in the above order and cut to a length of 40 mm X width 35 mm square The test piece was placed in a room with a relative humidity of 60% and a temperature of 23 ° C for 72, and then it was allowed to stand on a flat surface. Measure the height of the four corners. The value of the amount of bending is expressed as the average of 4 pieces of data. [Example 1] 4,7.5'-oxygen was dissolved in 407.5 g of N, N-dimethylformamide (DMF). 21.98 g of diphenylamine (ODA) and 7.91 g of p-phenylenediamine dissolution (PDA). Keep the solution at 0 ° C. Here, 29.47 g of 3,3 ', 4,4L benzophenonetetracarboxylic dianhydride (BTDA) was added slowly, and the mixture was stirred for 1 hour to completely dissolve the BTDA. To this solution was slowly added 25.15 g of p-phenylene bis (trimellitic acid monoester anhydride) (TMHQ), and after stirring for 1 hour, 7.98 g of pyromellitic dianhydride (PMDA) was added and stirred for 1 hour to obtain The solution at 23 ° C has a viscosity of 3000 poise and a solid concentration of 18.5% by weight. The mol% of the monomer component added at this time is shown in Table 1. In addition, in Table 1 and Table 3 described later, the monomer composition is described from the top stage to the next stage in the order of adding monomers. 100 g of the polyamic acid solution was mixed and stirred to contain 11.4 g of anhydrous acetic acid, 4.8 g of isoquinine, and 33.8 g of DMF as a hardener. The obtained solution was degassed by centrifugation, and then cast and coated on an aluminum foil. From stirring to degassing, cooling was performed simultaneously to 0 ° C. The laminated body of the aluminum foil and the polyamic acid solution was heated at 90 ° C for 600 seconds to obtain a self-supporting gel tape. The gel tape was detached from the aluminum foil and fixed to the frame. The gel strip was heated at 120 ° C, 250 ° C, 350 ° C, 450 ° C for 180 seconds each, and then heated in a far-infrared oven at 400 ° C for 180 seconds. Using this method, a 50 μm thick Polyurethane O: \ 87 \ 87969-940216.DOC -31-1243186 amine film was used to make a TAB tape according to the method described above. The elastic modulus, average linear expansion coefficient, hygroscopic expansion coefficient, and bending amount of the TAB tape of the polyimide film measured for the "copper tape" and "copper fully etched tape". The measurement results are shown in Table 2. [Example 2] 〇] 7.5 407.5 8 dissolves 00 八 17.9 008 and? 0-89.678, keep the solution at 0 ° C. Here, 28.81 g of BTDA was slowly added and stirred for 1 hour to completely dissolve the BTDA. To this solution was slowly added 24.59 g of TMHQ, and after stirring for 1 hour, 11.52 g of BTDA was added and stirred for 1 hour to obtain a polyamic acid solution having a solution viscosity of 2800 poise and a solid content concentration of 18.5 wt% at 23 ° C. The mol% of the monomer component added at this time is shown in Table 1. In addition, the mol% of BTDA in Table 1 is 50 and 20, which represent the amount of BPDA added initially and BPDA added later. A polyimide film and a TAB tape having a thickness of 50 µm were obtained in the same manner as in Example 1 except that the polyamic acid solution was used. The properties of the polyimide film and TAB tape are shown in Table 2. [Example 3] Dissolve 17.90 g of ODA and 9.67 g of PDA in 407.5 g of DMF, and keep the solution at 0 ° C. Here, 8.61 g of BTDA 3 was slowly added and stirred for 1 hour to completely dissolve the BTDA. To this solution, slowly add 24.59 g of TMHQ, and after stirring for 1 hour, add 1.73 g of BTDA and stir for 1 hour to obtain a polyamic acid solution with a viscosity of 3 10,000 poise and a solid concentration of 18.5 wt% at 23 ° C. . The mol% of the monomer component added at this time is shown in Table 1. Furthermore, the mol% of BTDA in Table 1 is 50 and 20, which represent the amount of BPDA added at the beginning of O: \ 87 \ 87969-9402t6.DOC -32-1243186 added afterwards. A polyimide film and a TAB tape having a thickness of 50 µm were obtained in the same manner as in Example 1 except that the polyamic acid solution was used. The properties of the polyimide film and TAB tape are shown in Table 2. [Example 4] 19.86 g of ODA and 8.77 g of PDA were dissolved in 407.5 g of DMF, and the solution was kept at 0 ° C. Here, 29.04 g of BTDA was slowly added and stirred for 1 hour to completely dissolve the BTDA. 28.92 g of TMHQ was slowly added to the solution, and after stirring for 1 hour, 5.90 g of PMDA was added, and the mixture was stirred for 1 hour to obtain a polyamic acid solution having a solution viscosity of 2900 poise and a solid content concentration of 18.5 wt% at 23 ° C. The mol% of the monomer component added at this time is shown in Table 1. A polyimide film and a TAB tape having a thickness of 50 µm were obtained in the same manner as in Example 1 except that the polyamic acid solution was used. The properties of the polyimide film and TAB tape are shown in Table 2. [Example 5] Dissolve 18.66 g of ODA and 10.07 g of PDA in 407.5 g of DMF, and keep the solution at 0 ° C. Here, 0.02 g of BTDA 3 was slowly added and stirred for 1 hour to completely dissolve the BTDA. 25.62 g of TMHQ was slowly added to the solution, and after stirring for 1 hour, 8.13 g of PMDA was added and stirred for 1 hour to obtain a polyamic acid solution having a viscosity of 3200 poise at 23 ° C and a solid content concentration of 18.5 wt%. The mol% of the monomer component added at this time is shown in Table 1. A polyimide film and a TAB tape having a thickness of 50 μm were obtained in the same manner as in Example 1 except that the polyamic acid solution was used. The properties of the polyimide film and TAB tape are shown in Table 2. O: \ 87 \ 87969-940216.DOC -33-1243186 [Example 6] Dissolve ODA 22.92 g and PDA 8.25 g in DMF 407.5 g, and keep the solution at 0 ° C. Here, 18.44 g of BTDA was slowly added and stirred for 1 hour to completely dissolve the BTDA. To this solution was slowly added 26.23 g of TMHQ, and after stirring for 1 hour, 16.65 g of PMDA was added and stirred for 1 hour to obtain a polyamic acid solution having a viscosity of 3000 poise and a solid content concentration of 18.5% by weight at 23 ° C. The monomer component mo 1 added at this time was 1 ° /. Shown in Table 1. A polyimide film and a TAB tape having a thickness of 50 μm were obtained in the same manner as in Example 1 except that the polyamic acid solution was used. The properties of the polyimide film and TAB tape are shown in Table 2. [Example 7] In DMF 407.5 g, 25.13 g of ODA and 7.31 g of PDA were dissolved, and the solution was kept at 0 ° C. Here, 12.44 g of BTDA was slowly added and stirred for 1 hour to completely dissolve the BTDA. To this solution was slowly added 26.55 g of TMHQ, and after stirring for 1 hour, 21.06 g of PMDA was added and stirred for 1 hour to obtain a polyamic acid solution having a viscosity of 3000 poise in 23 ^: and a solid content concentration of 18.5 wt%. The mol% of the monomer component added at this time is shown in Table 1. A polyimide film and a TAB tape having a thickness of 50 µm were obtained in the same manner as in Example 1 except that the polyamic acid solution was used. The properties of the polyimide film and TAB tape are shown in Table 2. [Example 8] Dissolve 18.86 g of ODA and 10.19 g of PDA in 407.5 g of DMF, and keep the solution at 0 ° C. Here, 11.09 g of 3,3f, 4,4'-biphenyltetracarboxylic dianhydride (BPDA) was slowly added and stirred for 1 hour to completely dissolve the BPDA. In this solution, O: \ 87 \ 87969-940216.DOC -34-1243186 was added with BTDA 18.22 g, and after stirring for 1 hour, TMHQ 25.91 g was added, stirred for 1 hour, and then PMDA 8.22 g was added. The solution has a viscosity of 2700 poise and a solid concentration of 18.5% by weight. The mol% of the monomer component added at this time is shown in Table 1. A polyimide film and a TAB tape having a thickness of 50 µm were obtained in the same manner as in Example 1 except that the polyamic acid solution was used. The properties of the polyimide film and TAB tape are shown in Table 2. [Comparative Example 1] Dissolve 21.48 g of ODA and 11.06 g of PDA in 407.5 g of DMF, and keep the solution at 0 ° C. Here, 31.56 g of BPDA was slowly added and stirred for 2 hours to completely dissolve the BPDA. 14.04 g of PMDA was slowly added to the solution, and after stirring for 1 hour, 13.83 g of BTDA was added and stirred for 1 hour to obtain a polyamic acid solution having a solution viscosity of 2800 poise and a solid content concentration of 18.5 wt% at 23 ° C. The mol% of the monomer component added at this time is shown in Table 3. A polyimide film and a TAB tape having a thickness of 50 µm were obtained in the same manner as in Example 1 except that the polyamic acid solution was used. The characteristics of the polyimide film and TAB tape are shown in Table 4. [Comparative Example 2] Dissolve 19.20 g of ODA and 10.37 g of PDA in 407.5 g of DMF, and keep the solution at 0 ° C. Here, slowly add 28.21 g of BPDA, for example, stir for 2 hours to completely dissolve the BPDA. To this solution, TMHQ 26.3 6 g was slowly added, and after stirring for 1 hour, 8.36 g of PMDA was added, and the mixture was stirred for 1 hour to obtain a polyamic acid solution having a solution viscosity of 2800 poise and a solid content concentration of 18.5% by weight at 23 ° C. The mol% of the monomer component added at this time is shown in Table 3. 〇: \ 87 \ 87969-940216. DOC -35-1243186 The polyimide film and TAB tape having a thickness of 50 µm were obtained in the same manner as in Example 1 except that this polyamic acid solution was used. The characteristics of the polyimide film and TAB tape are shown in Table 4. [Comparative Example 3] 19.92 g of ODA was dissolved in 407.5 g of DMF, and the solution was kept at 0 ° C. Here, 16.49 g of PMDA was slowly added and stirred for 1 hour to completely dissolve the PMDA. After dissolving 10.76 g of PDA in this solution, slowly add 17.57 g of BPDA and stir for 2 hours to completely dissolve BPDA. Furthermore, slowly add 26.45 g of TMHQ, stir for 1 hour, and then add 1.30 g of PMDA, and stir for 1 hour to obtain a polyamic acid with a viscosity of 3 100 poise at 23 ° C and a solid concentration of 18.5 wt% Solution. The mol% of the monomer component added at this time is shown in Table 3. And, the mol% of PMDA in Table 3 is 50 and 20, which represent the amount of PMDA added initially and BPDA added later. A polyimide film and a TAB tape having a thickness of 50 µm were obtained in the same manner as in Example 1 except that the polyamic acid solution was used. The characteristics of the polyimide film and TAB tape are shown in Table 4. [Comparative Example 4] 0.21 g of ODA3 and 5.15 g of PDA were dissolved in 407.5 g of DMF, and the solution was kept at 0 ° C. Here, TMHQ 26.39 g was slowly added, and after stirring for 1 hour, PMDA 3 0.75 g was added, and the mixture was stirred for 1 hour to obtain a polyamic acid solution having a solution viscosity of 2900 poise and a solid content concentration of 18.5 wt% at 23 ° C. . The mol% of the monomer component added at this time is shown in Table 3. A polyimide film and a TAB tape having a thickness of 50 µm were obtained in the same manner as in Example 1 except that the polyamic acid solution was used. The characteristics of polyimide film and TAB tape are shown in Table 4: O: \ 87 \ 87969-940216.DOC -36-1243186. [Comparative Example 5] 44.27 g of ODA was dissolved in 407.5 g of DMF, and the solution was kept at 0 ° C. Here, 48.23 g of PMDA was slowly added and stirred for 2 hours to completely dissolve the PMDA to obtain a polyamic acid solution having a viscosity of 2800 poise and a solid content concentration of 18.5% by weight in a solution at 23 ° C. The mol% of the monomer component added at this time is shown in Table 3. A polyimide film and a TAB tape having a thickness of 50 µm were obtained in the same manner as in Example 1 except that the polyamic acid solution was used. The characteristics of the polyimide film and TAB tape are shown in Table 4. [Comparative Example 6] Dissolve 24.87 g of ODA and 13.43 g of PDA in 407.5 g of DMF, and keep the solution at 0 ° C. Here, 54.19 g of PMDA was slowly added and stirred for 2 hours to completely dissolve the PMDA to obtain a polyamic acid solution having a viscosity of 2900 poise and a solid content concentration of 18.5 wt% in 231. The mol% of the monomer component added at this time is shown in Table 3. A polyimide film and a TAB tape having a thickness of 50 µm were obtained in the same manner as in Example 1 except that the polyamic acid solution was used. The characteristics of the polyimide film and TAB tape are shown in Table 4. [Comparative Example 7] Dissolve 26.19 g of ODA and 14.14 g of PDA in 489 g of DMF, and keep the solution at 0 ° C. At this point, 42.14 g of BTDA was slowly added, and after stirring for 1 hour, 28.53 g of PMDA was added slowly, and stirred for 2 hours to completely dissolve PMDA. The solution viscosity at 3,000 poise at 23 ° C and a solid concentration of 18.5 wt. % 〇: \ 87 \ 87969-940216.DOC -37-1243186 Polyamine solution. The mol% of the monomer component added at this time is shown in Table 3. A polyimide film and a TAB tape having a thickness of 50 µm were obtained in the same manner as in Example 1 except that the polyamic acid solution was used. The characteristics of the polyimide film and TAB tape are shown in Table 4. [Comparative Example 8] It is disclosed in the aforementioned Japanese Patent Application Publication No. 9-235373. The use of 3,3 ', 4,4'-benzophenone tetracarboxylic dianhydride as the acid component is the same as in Example 11. It is composed of monomers to obtain polyamic acid. The added weight of each monomer is 5.93 g of PPD, 11.64 g of PMDA, 2.97 g of ODA 3, 17.68 g of BTDA, and 24.28 g of PMDA. 〇The thickness of 50 μm was obtained in the same manner as in Example 1 except that the polyamic acid solution was used. When measuring the coefficient of hygroscopic expansion of a polyimide film, it is 18 ppm, which is a very large value. Therefore, the technique described in the above publication has not achieved a reduction in the coefficient of hygroscopic expansion. O: \ 87 \ 87969-940216.DOC 38-1243186 [Table 1] Example monomer composition (mol%) ODA PDA TMHQ BTDA PMDA BPDA 1 60 40 30 50 20 2 50 50 30 50 20 3 50 50 30 67 3 4 55 45 35 50 15 5 50 50 30 50 20 6 60 40 30 30 40 7 65 35 30 20 50 8 60 50 30 30 20 20 O: \ 87 \ 87969-940216.DOC -39- 1243186

亞胺膜於100°C至20〇t中之平均線膨脹係數為18 ppm/t: 以上、28 ppm/°C以下;彈性模數為4·5 GPa以上;吸濕膨脹係 數為13 ppm以下’作為關於本發明之聚醯亞胺膜,顯示優 越之物性。並且,於「附銅帶」之彎曲量,全部之實施例 為-0.5 mm以下,「全刻蝕」中之弯曲量亦全部之實施例為 2.0 mm以下,顯示可解決於加工及封裝步驟之彎曲而來之 不適點。 O:\87\87969-940216.DOC -40- 1243186 [表3] 比較例 單體組成(mol%) ODA PDA TMHQ BTDA PMDA BPDA 1 50 50 20 30 50 2 50 50 30 20 50 3 50 50 29 38 3 30 4 76 24 29 71 5 100 100 6 50 50 100 7 50 50 50 50 [表4] 比較例 凝膠 彈性模數 CTE CHE 彎曲,mm 揮發分 GPa ppm ppm 付銅 全蝕刻 1 40 5.6 19 14 1.0 1.7 2 55 膜溶化於鍛燒中 3 52 膜冒泡於鍛燒中 4 52 4.3 25 10 -2.5 2.4 5 47 3.1 32 12 -3.2 4.5 6 50 5.7 13 15 -2.7 1.6 7 50 5.7 13 15 -2.7 1.6 對此,如同顯示於表4一般,以比較例1〜7製造,被評價 之聚醯亞胺膜於100°C至200°C中之平均線膨脹係數、彈性 模數、吸濕膨脹係數其中之一未滿足上述(1)〜(3)之條件, O:\87\87969-940216.DOC -41 - 1243186 與有關本發明之聚醯亞胺膜比較,物性明顯低劣。並且, 於「附銅帶」中之彎曲量於比較例!、4、7為5咖以上,於 「全刻蝕」之彎曲量於比較例6為3111111以上,與有關本發明 之聚醢亞胺膜比較,物性低劣。 關於本發明之聚醯亞胺膜,如同以上一般,主要使用由 芳香族二胺與芳香族四羧酸二酐合成之聚醯胺酸所得之聚 醯亞胺膜,作為上述芳香族四羧酸二酐係包含3,3,,4,4,_二苯 甲酮四竣酸二酐之同時,於1〇〇U2〇(rc中之平均線膨服 係數為18 ppm/t:以上、28 ppm/t:以下;彈性模數為4 5 以上之同時,吸濕膨脹係數為13 ppm以下之者。 由此,兼具使彎曲及捲曲不發生之線膨脹係數及彈性模 數之同時,可提供亦不發生根據吸濕原因之尺寸變化之彎 曲及捲曲之聚醯亞胺膜。因此,於使用於各式各樣之電子 機器中之FPC及TAB帶之加工步驟中,可防止成為封裝不良 原因之彎曲及捲曲之發生之所謂效果奏效。 因此,本發明不僅係製造聚醯亞胺膜之化學產業及樹脂 產業,利用FPC及TAB帶等之電子零件產業,更且利用電子 零件之電氣、電子機器產業亦可適宜利用。 於發明詳細之說明之項中做出之具體之實施形態或實施 例’儘管終究本發明之技術内容為明確者,不應限定於該 等具體例而狹義解釋,於本發明之精神及其次記載之申請 專利範圍内,其為可多樣性變更、實施者。 O:\87\87969-940216.DOC -42-The average linear expansion coefficient of the imine film from 100 ° C to 20 ° t is 18 ppm / t: above, 28 ppm / ° C; the elastic modulus is above 4.5 GPa; and the coefficient of hygroscopic expansion is below 13 ppm 'As the polyimide film of the present invention, it has excellent physical properties. In addition, the bending amount in the "attached copper strip" is all below -0.5 mm, and the bending amount in "full etching" is all below 2.0 mm. It shows that it can be solved in the processing and packaging steps. Discomfort from bending. O: \ 87 \ 87969-940216.DOC -40-1243186 [Table 3] Comparative Example Monomer Composition (mol%) ODA PDA TMHQ BTDA PMDA BPDA 1 50 50 20 30 50 2 50 50 30 20 50 3 50 50 29 38 3 30 4 76 24 29 71 5 100 100 6 50 50 100 7 50 50 50 50 [Table 4] Comparative Example Gel Modulus CTE CHE Bend, mm Volatile GPa ppm ppm Full Copper Etching 1 40 5.6 19 14 1.0 1.7 2 55 Film melted during calcination 3 52 Film bubbled during calcination 4 52 4.3 25 10 -2.5 2.4 5 47 3.1 32 12 -3.2 4.5 6 50 5.7 13 15 -2.7 1.6 7 50 5.7 13 15 -2.7 1.6 In this regard, as shown in Table 4, the average linear expansion coefficient, elastic modulus, and hygroscopic expansion coefficient of the polyfluorene imine film evaluated at 100 ° C to 200 ° C were produced in Comparative Examples 1 to 7. One of them does not satisfy the conditions (1) to (3) above. O: \ 87 \ 87969-940216.DOC -41-1243186 Compared with the polyimide film of the present invention, the physical properties are obviously inferior. In addition, the amount of bending in "copper tape" is in a comparative example! , 4, and 7 are 5 or more, and the bending amount in "full etching" is 3111111 or more in Comparative Example 6. Compared with the polyimide film of the present invention, the physical properties are poor. As for the polyimide film of the present invention, as described above, a polyimide film obtained from a polyimide acid synthesized from an aromatic diamine and an aromatic tetracarboxylic dianhydride is mainly used as the aromatic tetracarboxylic acid. The dianhydride system contains 3,3,4,4, _benzophenonetetracarboxylic acid dianhydride, while the average linear expansion coefficient in RC is 18 ppm / t: above, 28 ppm / t: below; one with a modulus of elasticity of 4 5 or more and a coefficient of hygroscopic expansion of 13 ppm or less. Thus, it has both a coefficient of linear expansion and a modulus of elasticity that prevent bending and curling from occurring. Provides a polyimide film that does not undergo bending and curling due to dimensional changes due to moisture absorption. Therefore, it can prevent defective packaging during the processing steps of FPC and TAB tapes used in various electronic devices The so-called effect of the cause of bending and curling works. Therefore, the present invention is not only the chemical industry and resin industry for manufacturing polyimide film, the electronic component industry using FPC and TAB tape, etc., but also the electrical, Electronic equipment industry can also be used appropriately. The specific implementation form or embodiment made in the item of the detailed description 'Although the technical content of the present invention is clear, it should not be limited to these specific examples and should be interpreted narrowly. Within the scope of the patent, it can be changed and implemented by diversity. O: \ 87 \ 87969-940216.DOC -42-

Claims (1)

12431861243186 拾、申請專利範園: 一種聚醯亞胺膜,其係主要使用由芳香族二胺及芳香族 四竣酸二酐合成之聚酿胺酸而得者, 於100〜200°c下之平均線膨脹係數為^〜“卯瓜,彈 性模數為4.5 GPa以上,吸濕膨脹係數為13 ppm以下, 作為芳香族四羧酸二酐,係使用3,3,,4,4,_二苯甲_四 羧酸二酐作為必須成分。 2·如申請專利範圍第1項之聚醯亞胺膜,其中將全芳香族 四羧酸一酐成分設為100 m〇l〇/〇時,係使用2〇〜6〇 範圍内之3,3,,4,4’-二苯甲_四魏酸二肝。 3 ·如申請專利範圍第2項之聚醯亞胺膜,其中進一步使用 芳香族Sg酸一 gf作為上述芳香族四竣酸二野成分。 4·如申請專利範圍第3項之聚醯亞胺膜,其中當全芳香族 四羧酸二酐成分設為1〇〇 m〇1%時,係使用1〇〜6〇 範圍内之上述芳香族酯酸二酐。 5·如申請專利範圍第3項之聚醯亞胺膜,其中使用對伸笨 基雙(偏苯三酸單酯酐)作為上述芳香族酯酸二酐。 6·如申請專利範圍第丨項之聚醯亞胺膜,其中使用各自至 少1種直線性二胺及彎曲性二胺作為上述芳香族二胺成 分0 7·如申請專利範圍第6項之聚醯亞胺膜,其中將全芳香族 二胺成分設為1〇〇 m〇l%之時,使用各自於2〇〜8〇 之範圍内及80〜20 mol%之1種以上範圍内之上述直線 性二胺及彎曲性二胺。 O:\87\87969-940216.DOC 1243186 亞胺膜,其中使用對苯二 8·如申請專利範圍第6項之聚醯 胺作為上述直線性二胺。 9 ·如申清專利範圍第6項之聚酸 苯胺作為上述彎曲性二胺。 亞胺膜,其中使用4,4,-氧二 一月安0 10·如申請專利範圍第6項之聚醯亞胺膜Fanyuan Garden: A polyimide film, which is mainly obtained by using polyamino acid synthesized from aromatic diamine and aromatic quaternary acid dianhydride. The average value at 100 ~ 200 ° c The linear expansion coefficient is ^ ~ ", the elastic modulus is 4.5 GPa or more, and the hygroscopic expansion coefficient is 13 ppm or less. As the aromatic tetracarboxylic dianhydride, 3,3,, 4,4, _dibenzene is used. Formic acid tetracarboxylic dianhydride is an essential component. 2. The polyimide film according to item 1 of the scope of patent application, in which the total aromatic tetracarboxylic monoanhydride component is set to 100 m0 / 0, Use 3,3,4,4'-Dibenzoyl-tetraweilic acid diliver in the range of 20 to 60. 3. The polyimide film according to item 2 of the patent application, wherein aromatics are further used. Sg acid mono-gf is used as the above-mentioned aromatic tetramethylene acid two-field component. 4. The polyimide film according to item 3 of the patent application scope, wherein when the wholly aromatic tetracarboxylic dianhydride component is set to 1000 m01 %, The above-mentioned aromatic ester acid dianhydride in the range of 10 to 60 is used. 5. The polyimide film according to item 3 of the patent application, wherein (Trimellitic acid monoester anhydride) as the above-mentioned aromatic ester acid dianhydride. 6. The polyimide film according to item 丨 of the application, wherein at least one linear diamine and flexible diamine are used as each. The above aromatic diamine component is the polyimide film according to item 6 of the patent application, wherein when the total aromatic diamine component is set to 100 mol%, each is used at 20 to 8 The above-mentioned linear diamine and flexible diamine in the range of 〇 and in one or more ranges of 80 to 20 mol%. O: \ 87 \ 87969-940216.DOC 1243186 imine film, in which terephthalic acid 8 · For example, the polyamine in the scope of the application for the patent No. 6 is used as the above-mentioned linear diamine. 9 · The polyaniline in the scope of the patent application for the No. 6 is used as the above-mentioned flexible diamine. The imine film, which uses 4,4,- Oxygen carbamide 0 10 · As for the polyimide film of scope 6 of the patent application 亞胺分子中。 應而得聚酿胺酸溶液之步驟, b)於支持體上澆鑄包含上述聚醯胺酸溶液之製膜膠漿之 亞胺膜,其卡上述直線性 製造方法,至少包含: 使芳香族二胺及芳香族四羧酸二酐反 步驟, c)於支持體上加熱上述製膜膠漿之後,從支持體拆離凝 膠膜之步驟, d)再加熱砝膠膜,使殘存之醯胺酸醯亞胺化,使之乾燥 之步驟, 且使用3,3’,4,4、二苯甲酮四羧酸二酐及芳香族酯酸二 酐作為上述芳香族四羧酸二酐, 將全芳香族四羧酸二酐成分設為1〇〇 mol%時,使用 20-60 m〇i%範圍内之3,3»,4,4’-二苯曱酮四羧酸二酐,使 用10-60 m〇l%範圍内之芳香族酯酸二酐。 12·如申請專利範圍第u項之聚醯亞胺膜之製造方法,其中 使用對伸苯基雙(偏苯三酸單酯酐)作為上述芳香族酯酸 二酐。 13.如申請專利範圍第u項之聚醯亞胺膜之製造方法,其中 O:\87\87969-940216.DOC -2 - 1243186 使用各自至少1種之直線性二胺及彎曲性二胺作為上述 芳香族二胺成分。 14·如申4專利範圍第13項之聚酿亞胺膜之製造方法,其中 等王务曰方矢一胺成分設為1〇〇 m〇i%時,使用各自於2〇 〜80 m〇l%之範圍内及80〜20 mol%範圍内之上述直線 性二胺及彎曲性二胺。 15·如申晴專利範圍第u項之聚醯亞胺膜之製造方法,其中 至少併用脫水劑及酿亞胺化觸媒。 16· —種FC帶,其係於一聚醯亞胺膜上設置黏著劑層及保護 層而成者,其中該聚醯亞胺膜係使用藉由使聚醯胺酸經 醯亞胺化而彳于之聚醯亞胺所成者,而作為聚酸胺酸之原 料之S文成分及二胺成分,係分別使用至少於結構中含芳 香%結構之芳香族四羧酸成分及芳香族二胺成分, 再者,作為上述聚醯胺酸之原料中之芳香族四羧酸成 刀,係至少使用二苯甲酮四羧酸二酐作為必須 成分, 該聚醯亞胺膜於丨00〜200艺下之平均線膨脹係數為 18〜28卯111,吸濕膨脹係數為13卯111以下,且彈性模數 為4.5 GPa以上。 1 7· —種撓性印刷電路板,其係至少包含一聚醯亞胺膜組成 之層及金屬導電層,該聚醯亞胺膜係使用藉由使聚醯胺 酸經醯亞胺化而得之聚醯亞胺所成者,而作為聚醯胺酸 之原料之酸成分及二胺成分,係分別使用至少於結構中 含芳香環結構之芳香族四羧酸成分及芳香族二胺成分, O:\87\87969-940216.DOC -3- 1243186 再者,作為上述聚醢胺酸之原料中之芳香族四羧酸成 分,係至少使用3,3,,4,4,-二苯甲酮四羧酸二酐作為必須 成分, 該聚醯亞胺膜於100〜20(rc下之平均線膨脹係數為 18〜28Ppm,吸濕膨脹係數為^卯瓜以下,且彈性模數 為4.5 GPa以上。 O:\87\87969-940216.DOC 4-Imine molecule. The step of obtaining a polyamino acid solution accordingly, b) casting the imine film of the film-forming paste containing the polyamino acid solution on a support, the card linear manufacturing method described above, including at least: Amine and aromatic tetracarboxylic dianhydride reverse steps, c) the step of detaching the gel film from the support after heating the film-forming glue on the support, d) heating the weight film to make the remaining amidine A step of imidizing and drying the acid, and using 3,3 ', 4,4, benzophenone tetracarboxylic dianhydride and an aromatic ester acid dianhydride as the aromatic tetracarboxylic dianhydride, When the total aromatic tetracarboxylic dianhydride component is set to 100 mol%, 3,3 », 4,4'-benzophenone tetracarboxylic dianhydride in the range of 20-60 m% is used. Aromatic ester dianhydride in the range of 10-60 mol%. 12. The method for producing a polyimide film according to item u of the application, wherein p-phenylene bis (trimellitic acid monoester anhydride) is used as the aromatic ester acid dianhydride. 13. A method for manufacturing a polyimide film according to item u of the application, wherein O: \ 87 \ 87969-940216.DOC-2-1243186 uses at least one of linear diamine and flexible diamine, respectively. The aromatic diamine component. 14. The method for manufacturing a polyimide film according to item 13 of the scope of the patent of claim 4, wherein when the composition of Wangyao Fangya Monoamine is set to 100%, use each of 20 ~ 80m. The above-mentioned linear diamine and flexible diamine in the range of 1% and in the range of 80 to 20 mol%. 15. A method for manufacturing a polyimide film as described in item u of the Shenqing patent, wherein at least a dehydrating agent and an imidization catalyst are used in combination. 16. · A type of FC tape, which is formed by providing an adhesive layer and a protective layer on a polyimide film, wherein the polyimide film is obtained by subjecting a polyimide to a polyimide It is made of polyimide, and the S component and the diamine component as the raw material of the polyamic acid are the aromatic tetracarboxylic acid component and the aromatic two The amine component, in addition, the aromatic tetracarboxylic acid used as the raw material of the polyamic acid is a knife, and at least benzophenone tetracarboxylic dianhydride is used as an essential component. The average linear expansion coefficient at 200 times is 18 ~ 28 卯 111, the hygroscopic expansion coefficient is 13 卯 111 or less, and the elastic modulus is 4.5 GPa or more. 1 ·· A flexible printed circuit board comprising at least a layer composed of a polyimide film and a metal conductive layer. The polyimide film is obtained by subjecting a polyimide to a polyimide. Those obtained from polyimide, and the acid component and diamine component of the raw material of polyamidic acid, respectively, use an aromatic tetracarboxylic acid component and an aromatic diamine component containing an aromatic ring structure in the structure. , O: \ 87 \ 87969-940216.DOC -3- 1243186 In addition, as the aromatic tetracarboxylic acid component in the raw material of the above polyamic acid, at least 3,3,4,4, -dibenzene is used. Methyl ketone tetracarboxylic dianhydride is an essential component. The average linear expansion coefficient of the polyimide film at 100 to 20 (rc is 18 to 28 Ppm, the coefficient of hygroscopic expansion is less than or equal to, and the elastic modulus is 4.5. GPa or higher. O: \ 87 \ 87969-940216.DOC 4-
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