TW200948862A - Polyester-imide precursor and polyester-imide - Google Patents

Polyester-imide precursor and polyester-imide Download PDF

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TW200948862A
TW200948862A TW097135365A TW97135365A TW200948862A TW 200948862 A TW200948862 A TW 200948862A TW 097135365 A TW097135365 A TW 097135365A TW 97135365 A TW97135365 A TW 97135365A TW 200948862 A TW200948862 A TW 200948862A
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polyester
precursor
formula
temperature
quinone imine
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TW097135365A
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TWI395770B (en
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Akihiro Kato
Toru Koizumi
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Asahi Chemical Ind
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Priority claimed from JP2008130045A external-priority patent/JP2009275183A/en
Priority claimed from JP2008212101A external-priority patent/JP2010047674A/en
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    • 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
    • H05K1/0313Organic insulating material
    • H05K1/032Organic insulating material consisting of one material
    • H05K1/0326Organic insulating material consisting of one material containing O
    • 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
    • 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
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/28Layered products comprising a layer of synthetic resin comprising synthetic resins not wholly covered by any one of the sub-groups B32B27/30 - B32B27/42
    • B32B27/281Layered products comprising a layer of synthetic resin comprising synthetic resins not wholly covered by any one of the sub-groups B32B27/30 - B32B27/42 comprising polyimides
    • 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
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/36Layered products comprising a layer of synthetic resin comprising polyesters
    • 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
    • C08G73/16Polyester-imides
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L79/00Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen or carbon only, not provided for in groups C08L61/00 - C08L77/00
    • C08L79/04Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
    • C08L79/08Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
    • 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
    • H05K1/0313Organic insulating material
    • H05K1/032Organic insulating material consisting of one material
    • H05K1/0346Organic insulating material consisting of one material containing N
    • 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
    • B32B2307/00Properties of the layers or laminate
    • B32B2307/30Properties of the layers or laminate having particular thermal properties
    • B32B2307/306Resistant to heat
    • B32B2307/3065Flame resistant or retardant, fire resistant or retardant
    • 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
    • B32B2307/00Properties of the layers or laminate
    • B32B2307/50Properties of the layers or laminate having particular mechanical properties
    • 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
    • B32B2307/00Properties of the layers or laminate
    • B32B2307/50Properties of the layers or laminate having particular mechanical properties
    • B32B2307/582Tearability
    • B32B2307/5825Tear resistant
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2457/00Electrical equipment
    • B32B2457/08PCBs, i.e. printed circuit boards
    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05KPRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K2201/00Indexing scheme relating to printed circuits covered by H05K1/00
    • H05K2201/01Dielectrics
    • H05K2201/0137Materials
    • H05K2201/0145Polyester, e.g. polyethylene terephthalate [PET], polyethylene naphthalate [PEN]
    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05KPRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K2201/00Indexing scheme relating to printed circuits covered by H05K1/00
    • H05K2201/01Dielectrics
    • H05K2201/0137Materials
    • H05K2201/0154Polyimide

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

Abstract

A polyester-imide precursor characterized by having repeating units represented by the following formula (1). (In the formula (1), Ar is the tetravalent aromatic group represented by the formula (2) and B1 is an ester structure having a specific structure.)

Description

200948862 九、發明說明: 【發明所屬之技術領域】 本發明係關於一種可撓性印刷配線板等積層板中所使用 之聚酯醯亞胺前驅物及聚酯酿亞胺》 【先前技術】 由於聚醯亞胺不僅具有優異的財熱性而且兼具耐化學 ‘ 性、耐輻射性、電氣絕緣性、優異的機械性質等特性,因 此被廣泛應用於FPC(Flexible Printed Circuit,可撓性印刷 © 電路)基板、TAB(Tape Automated Bonding,捲帶式自動接 合)用基材、半導體元件之保護膜、積體電路之層間絕緣 膜等各種電子裝置中。又,聚醯亞胺除該等特性以外,因 具有製造方法的簡便性、極高的膜純度,故近年來其重要 性愈來愈增強。 隨著電子機器趨向於輕薄短小化,對於聚酿亞胺之特性 要求亦一年年地嚴格起來’因而業界正在尋求一種不僅具 0 有焊錫耐熱性’而且同時滿足聚醯亞胺膜針對熱循環或吸 濕的尺寸穩定性、透明性、與金屬基板的接著強度、成形 加工性、通孔等微細加工性等多個特性之多功能性聚醯亞 胺材料。 近年來’對作為FPC基板之聚醯亞胺的需求飛速地增 加。作為FPC的原板之鋼箔積層板及F<:CL(Flexible Copper Clad Laminate ’軟性銅箔基板)之構成主要分類為3種樣 式。即,已知有1)利用環氧系接著劑等將聚醯亞胺層(以下 亦稱為「聚醯亞胺膜」)與銅箔進行貼附之3層型,2)在向 134489.doc 200948862 銅箔上塗布聚醯亞胺溶液後進行乾燥或者在塗布聚醯亞胺 前驅物溶液後進行乾燥、醯亞胺化,或者藉由蒸鑛、濺鍍 等於聚酿亞胺層上形成銅層之無接著劑2層型,3 )使用熱 塑性聚醯亞胺作為接著層之偽2層型。若係要求聚醯亞胺 層具有高度的尺寸穩定性之用途,則以不使用接著劑之2 層FCCL較為有利。 作為FPC基板之聚酿亞胺’因曝露於封裝步驟中的各種 熱循環中因而會產生尺寸變化。為了儘量抑制該現象,較 好的是聚醯亞胺之玻璃轉移溫度(Tg)高於步驟溫度,此外 聚醯亞胺於玻璃轉移溫度以下之線熱膨脹係數儘可能地 低’且聚醯亞胺與金屬箔之線熱膨脹係數相匹配。如下所 述,就降低於2層FCCL製造步驟中所產生的殘留應力之觀 點而言’對聚醯亞胺層之線熱膨脹係數的控制亦為重要。 又,就安全性之觀點而言,業者希望開發出一種高阻燃性 之聚醯亞胺用於FPC基板。 因多數聚醯亞胺不溶於有機溶劑、且即使於玻璃轉移溫 度以上亦不會熔融,故對聚醯亞胺本身進行成形加工通常 並不容易。因此’聚醯亞胺通常是使等莫耳的均苯四甲酸 二酐(PMDA)等芳香族四羧酸二酐與4,4,-二胺基二笨喊 (ODA)等芳香族二胺於二曱基乙醯胺(DMAc)等非質子性極 性有機溶劑中反應,貧先使高聚合度的聚醯亞胺前驅物溶 液聚合’再將該聚醯亞胺前驅物溶液塗布於金屬箔例如鋼 洎上,於2501:〜40(TC下加熱進行脫水閉環(醯亞胺化), 而進行製臈。 134489.doc 200948862 殘留應力係在高溫下的醯亞胺化反應後,使金屬/聚醯 亞胺積層板冷卻至室溫之過程中產生,經常會引起FCCL 的^制離'媒破裂等嚴重問題。X,於使用聚酿亞胺 溶液之情形時’於乾燥-冷卻步驟中,亦與使用聚醯亞胺 前驅物溶液時同樣會產生殘留應力之問題。 作為降低殘留應力之措施,有效方法是使作為絕緣膜之 聚酿亞胺本身的線熱膨脹係數降低。絕大部分之聚醯亞胺 的線熱膨脹係數係在40 ppm/t〜1〇〇 ppm/t之範圍内,遠 遠大於金屬箔例如銅箔的線熱膨脹係數17 ppm/〇c,因此 業者正在研究開發線熱膨脹係數接近於銅箔之值顯示大約 20 ppm/°C以下的線熱膨脹係數之聚醯亞胺。 目前’作為實用的聚醢亞胺材料,熟知有由3,3,,4,4,_聯 苯四甲酸二酐與對苯二胺所形成之聚醯亞胺.該聚醯亞胺 膜亦根據膜厚或製作條件而顯示5 ppm/°C〜10 ppm/°C之非 常低的線熱膨脹係數,但並不顯示低吸濕膨脹係數(參照 非專利文獻1)。 要求聚醯亞胺不僅對於熱循環具有尺寸穩定性而且對於 吸濕亦具有尺寸穩定性。先前之聚醯亞胺亦吸濕2質量%〜 3質量%的水。與由於絕緣層吸濕所造成的尺寸變化同時 發生之電路位置偏移,對於高密度配線或多層配線而言係 嚴重的問題。由於電特性之下降,因而會引起聚醯亞胺/導 體界面上之腐银(Corrosion)、離子遷移、絕緣破壞等更嚴 重問題之虞。因此,要求作為絕緣膜之聚醯亞胺層的吸濕 膨脹係數儘可能地低。 134489.doc 200948862 為了實現低吸濕膨脹係數,例如報告有使用以式(20)所 表示的骨架中具有醋結構的酸二酐之聚酯醯亞胺係有效者 (參照專利文獻1): [化1]。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 48 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯 醯Polyimine is widely used in FPC (Flexible Printed Circuit) because it has excellent heat and chemical resistance, radiation resistance, electrical insulation, and excellent mechanical properties. In various electronic devices such as a substrate, a substrate for TAB (Tape Automated Bonding), a protective film for a semiconductor element, and an interlayer insulating film for an integrated circuit. Further, in addition to these properties, polyimine has an increase in the importance of the production method and extremely high film purity. As electronic devices tend to be lighter and shorter, the characteristics of the poly-imine are also stricter year after year. "Therefore, the industry is looking for a solder heat resistance that is not only 0, but also meets the thermal cycle of the polyimide film. A multifunctional versatile polyimide material having a plurality of properties such as dimensional stability, transparency, adhesion strength to a metal substrate, moldability, and fine workability such as through-hole. In recent years, the demand for polyimine as an FPC substrate has rapidly increased. The steel foil laminated sheets of the original FPC and the F::CL (Flexible Copper Clad Laminate 'soft copper foil substrate) are mainly classified into three types. In other words, a three-layer type in which a polyimide layer (hereinafter also referred to as "polyimine film") and a copper foil are attached by an epoxy-based adhesive or the like is known, and 2) is in the direction of 134489. Doc 200948862 Copper foil coated with polyimide solution, dried or coated with polyimide precursor solution, dried, yttrium imidized, or formed by copper ore and sputtered to form copper on the polyimide layer The layer has no adhesive 2 layer type, and 3) a thermoplastic polyimide is used as the pseudo 2-layer type of the adhesive layer. If the polyimine layer is required to have a high dimensional stability, it is advantageous to use a two-layer FCCL without an adhesive. The size of the polyienimine as an FPC substrate is caused by exposure to various thermal cycles in the encapsulation step. In order to suppress this phenomenon as much as possible, it is preferred that the glass transition temperature (Tg) of the polyimide is higher than the step temperature, and further, the linear thermal expansion coefficient of the polyimine at a glass transition temperature is as low as possible and the polyimine Matches the coefficient of thermal expansion of the metal foil. As described below, it is also important to control the linear thermal expansion coefficient of the polyimide layer in terms of reducing the residual stress generated in the 2-layer FCCL manufacturing step. Further, from the viewpoint of safety, the industry has hoped to develop a highly flame-retardant polyimine for use in an FPC substrate. Since most of the polyimine is insoluble in an organic solvent and does not melt even above the glass transition temperature, it is generally not easy to form the polyimine itself. Therefore, 'polyimine is usually an aromatic tetracarboxylic dianhydride such as equimolar pyromellitic dianhydride (PMDA) and an aromatic diamine such as 4,4,-diaminodiphenyl (ODA). Reacting in an aprotic polar organic solvent such as dimercaptoacetamide (DMAc), preliminarily polymerizing a solution of a high degree of polymerization of a polyamidene precursor, and then applying the solution of the polyimide precursor to the metal foil For example, on steel shovel, at 2501:~40 (heating under TC for dehydration ring closure (醯imination), 臈 臈 134489.doc 200948862 Residual stress is caused by yttrium imidization at high temperature, making metal / The polyimide polyimide laminate is produced during the process of cooling to room temperature, which often causes serious problems such as FCCL cracking. X, in the case of using the brewing solution, 'in the drying-cooling step, It also causes residual stress problems when using a polyimide precursor solution. As a measure to reduce residual stress, an effective method is to reduce the linear thermal expansion coefficient of the polyaniline itself as an insulating film. The linear thermal expansion coefficient of ruthenium is 40 ppm/t~1〇 In the range of ppm/t, which is much larger than the linear thermal expansion coefficient of metal foil such as copper foil of 17 ppm/〇c, the industry is investigating the development of linear thermal expansion coefficient close to the value of copper foil showing linear thermal expansion of about 20 ppm/°C or less. Copolyimine of the coefficient. At present, as a practical polyimine material, a polyimine formed from 3,3,4,4,4-biphenyltetracarboxylic dianhydride and p-phenylenediamine is well known. The polyimine film also exhibits a very low linear thermal expansion coefficient of 5 ppm/° C. to 10 ppm/° C. depending on the film thickness or the production conditions, but does not exhibit a low hygroscopic expansion coefficient (see Non-Patent Document 1). Polyimine is required to have dimensional stability not only for thermal cycling but also dimensional stability for moisture absorption. Previous polybenzamine also absorbs 2% by mass to 3% by mass of water. The resulting circuit position shift occurs at the same time, which is a serious problem for high-density wiring or multilayer wiring. Due to the decrease in electrical characteristics, it causes rosin (Corrosion) on the polyimide/conductor interface. Ion migration, insulation damage, etc. are more stringent Therefore, the hygroscopic expansion coefficient of the polyimide layer as the insulating film is required to be as low as possible. 134489.doc 200948862 In order to achieve a low hygroscopic expansion coefficient, for example, the report is expressed by the formula (20). The polyester bismuth imino group having an acid dianhydride having a vinegar structure is effective (see Patent Document 1): [Chemical Formula 1]

〈20) 0 ❹ 然而,一般認為,為了實現低吸濕膨脹係數而使用通式 (20)作為酸二酐並使用式(21)〜式(23)作為二胺所製作之聚 酯醯亞胺膜’因二胺具有高彎曲結構,故不僅具有高線熱 膨脹係數而且由該等的組合所構成之聚酯醯亞胺膜成為可 燃性膜: [化2]<20) 0 ❹ However, it is generally considered that a polyester quinone imine prepared by using the formula (20) as an acid dianhydride and using the formula (21) to the formula (23) as a diamine in order to achieve a low moisture absorption coefficient is considered. Since the film has a highly curved structure, the film has not only a high coefficient of thermal expansion but also a polyester phthalimide film composed of these combinations as a flammable film: [Chemical 2]

[化3] ❹[化3] ❹

(2 2) [化4](2 2) [Chemical 4]

(23) 此處’若使用如式(24)之具有剛性結構之二胺作為二 胺,則具有低線熱膨脹係數,但由於其剛性而具有高彈性 134489.doc 200948862 率,因而並不適於要求低排斥性之用途,進而推測接著性 (與金屬箔之剝離強度)會下降: [化5] W (24)。 因此,進而亦報告有使用以式(19)所表示之酸二酐(以下 稱為TABP)之聚酯醯亞胺(參照專利文獻2): [化6] ❹ ❹(23) Here, if a diamine having a rigid structure such as formula (24) is used as the diamine, it has a low coefficient of thermal expansion, but has a high elasticity due to its rigidity, and is therefore not suitable for the requirement. For the use of low repellency, it is presumed that the adhesion (peeling strength with metal foil) will decrease: [Chem. 5] W (24). Therefore, a polyester phthalimide using an acid dianhydride represented by the formula (19) (hereinafter referred to as TABP) has been reported (refer to Patent Document 2): [Chemical Formula 6] ❹ ❹

(19) 〇 記載有專利文獻2中所揭示之利用二胺與上述酸二酐所 獲得之聚醋醯亞胺同時達成低熱膨脹係數與低吸水性 (1.2%〜1.9%)。然而,一般認為吸水率為12%之聚酯醯亞 胺膜難以滿足低吸濕膨脹係數(8 ppm/% RH以下,3〇〇/0 RH〜70% RH)之要求。又,於由薄膜聚醯亞胺膜所構成之 FPC基板的加工步驟中’為了避免由於聚酿亞胺膜破裂所 造成的良率下降,則要求聚醯亞胺膜具有高撕裂強度,但 上述文獻並未揭示撕裂強度。又,一般認為以所記載之聚 酯醯亞胺的組成無法達成高撕裂強度。又,一般認為,因 使用如式(21)或式(25)的彎曲性分子,故玻璃轉移溫度亦 較低: [化7] 134489.doc (21) •10- 200948862 [化8] 另一方面’亦報告有使用二胺中具有酯結構的化合物之 . 聚醋醢亞胺(參照專利文獻3)。然而,仍然認為此情形亦與 上述同樣無法獲得高撕裂強度。 又’亦有可能產生由於使用TABP所造成之異常。製造 ❹ 具有酯結構之酸二酐的通常方法,已知有:於苯或甲苯令 使偏苯二甲酸肝醯氣(trime⑴tic anhydride chloride)與二醇 反應之方法(專利文獻4),或酚類的低級烷酸酯與偏苯三甲 酸酐之醋交換反應(專利文獻5);利用該等方法可獲得 TABP之粗結晶。然而,若使用所得粗結晶使其與芳香族 一胺發生共聚合,則所得聚醯亞胺前驅物溶液的一部分會 發生凝膠化,又,若使用該聚醯亞胺前驅物溶液來製作聚 醯亞胺膜,則有可能產生聚醯亞胺膜的機械物性明顯下降 ❹ 之異常。 如此,在分子設計上不易獲得在保持聚合反應性或製膜 加工性的狀態下兼具與銅落同等的低線熱膨脹係數、高阻 燃性、低吸濕膨脹係數(8 ppm/% RH以下,3〇% RH7〇% RH)、可撓性、焊錫耐熱性、高玻璃轉移溫度、高接著 性、低彈性率而且達成高撕裂強度之聚酿亞胺,目前為止 尚未知悉有滿足此種要求特性之實用材料。 ’ [專利文獻1]日本專利特開平1〇_7〇157號公報 134489.doc 200948862 [專利文獻2]曰本專利特開2〇〇6_336〇11號公報 [專利文獻3]曰本專利3712164號公報 [專利文獻4]曰本專利特公昭43·5911號公報 [專利文獻5]曰本專利特開平〇7_41472號公報 [非專利文獻 l]Macr〇molecules,29,7897(1996) 【發明内容】 [發明所欲解決之問題] ❹ 本發明係蓉於上述問題而完成者,本方面之目的在於提 供一種兼具高阻燃性、低吸濕膨脹係數、與銅箔同等的低 線熱膨脹係數、高玻璃轉移溫度、高接著性、低彈性率、 局撕裂強度之聚醋酿亞胺。 [解決問題之技術手段] 本發明之聚酯醯亞胺前驅物,其特徵在於:具有以下述 式(1)所表示之重複單元: [化9](19) 聚 The polyacetamide obtained by using the diamine and the acid dianhydride disclosed in Patent Document 2 simultaneously exhibits a low coefficient of thermal expansion and a low water absorption (1.2% to 1.9%). However, it is generally considered that a polyesterimine film having a water absorption of 12% is difficult to satisfy the requirement of a low hygroscopic expansion coefficient (below 8 ppm/% RH, 3 〇〇/0 RH to 70% RH). Further, in the processing step of the FPC substrate composed of the thin film polyimide film, in order to avoid a decrease in yield due to cracking of the polyimide film, the polyimide film is required to have high tear strength, but The above documents do not disclose the tear strength. Further, it is considered that the composition of the polyester phthalimide described above cannot achieve high tear strength. Further, it is generally considered that the glass transition temperature is also low due to the use of a bending molecule such as the formula (21) or the formula (25): [Chem. 7] 134489.doc (21) • 10- 200948862 [Chem. 8] In the aspect, a compound having an ester structure in a diamine is also reported. Polyacetal imine (see Patent Document 3). However, it is still considered that this situation is also incapable of obtaining high tear strength as described above. Also, it is also possible to generate anomalies caused by the use of TABP. A general method for producing an acid dianhydride having an ester structure is known as a method for reacting diol or toluene to dimethyl alcohol (trime(1) tic anhydride chloride) with a diol (Patent Document 4), or a phenol. The vinegar exchange reaction of the lower alkanoate with trimellitic anhydride (Patent Document 5); the crude crystal of TABP can be obtained by these methods. However, if the obtained crude crystal is used to copolymerize with an aromatic monoamine, a part of the obtained polyimine precursor solution may be gelated, and if the polyimine precursor solution is used to prepare a poly In the case of the quinone imine film, there is a possibility that the mechanical properties of the polyimide film are significantly lowered. In this way, it is difficult to obtain a low linear thermal expansion coefficient, a high flame retardancy, and a low hygroscopic expansion coefficient (8 ppm/% RH or less) equivalent to copper drop in the state of maintaining polymerization reactivity or film forming workability. , 3〇% RH7〇% RH), flexibility, solder heat resistance, high glass transition temperature, high adhesion, low modulus of elasticity and high tear strength of the brewed imine, so far no known to meet this Practical materials that require characteristics. [Patent Document 1] Japanese Patent Laid-Open Publication No. Hei No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. [Patent Document 4] Japanese Patent Laid-Open Publication No. Hei. No. Hei. No. Hei 7-41472 (Non-Patent Document 1) Macr〇molecules, 29,7897 (1996) [Summary of the Invention] [Problems to be Solved by the Invention] The present invention has been completed in view of the above problems, and an object of the present invention is to provide a low-line thermal expansion coefficient which is high in flame retardancy, low in hygroscopic expansion coefficient, and equivalent to copper foil. High glass transition temperature, high adhesion, low modulus of elasticity, and local tear strength of the polyacetal. [Technical means for solving the problem] The polyester quinone imine precursor of the present invention has a repeating unit represented by the following formula (1): [Chemical 9]

L 8L 8

⑴ (式(1)中,Ar為以式(2)所表示之4價芳香族基,B!為邊 自式(3)〜式(9)中之至少一種之2價芳香族基: [化 10](1) In the formula (1), Ar is a tetravalent aromatic group represented by the formula (2), and B! is a divalent aromatic group derived from at least one of the formulae (3) to (9): 10]

134489.doc (2) -12· 200948862 [化η] [化 12] ❹ [化 13] [化 14] [化 15] [化 16] 134489.doc (9) 200948862 [化 17]134489.doc (2) -12· 200948862 [化η] [Chemical 12] ❹ [Chem. 13] [Chem. 14] [Chem. 15] [Chem. 16] 134489.doc (9) 200948862 [Chem. 17]

A表示碳數1〜6之燒基¥表示碳數卜6之院基、氫 原子,、遠等為分別獨立,可相同亦可不同;&amp;表示碳數 1〜6之烷基,r6〜R4示碳數卜6之烷基、氫原子)。 ❹A represents a carbon number of 1 to 6 and a base of a carbon number of 6 represents a carbon number of 6 and a hydrogen atom. The distance is independently independent, and may be the same or different; &amp; represents an alkyl group having a carbon number of 1 to 6, r6~ R4 represents an alkyl group of a carbon number of 6, and a hydrogen atom). ❹

於本發明之聚㈣亞胺前驅物中,上述聚㈣亞胺前驅 物中’式⑴中之Bl較好較以式(3)或式⑷所表示之重複 單元’進而較好的是以式(4)所表示之重複單元,尤其妤的 是式(4)中R_2〜尺4選擇氫原子之式(1〇): [化 18]In the poly(tetra)imine precursor of the present invention, the B1 in the formula (1) in the poly(tetra)imine precursor is preferably a repeating unit represented by the formula (3) or the formula (4), and further preferably (4) The repeating unit represented, in particular, the formula (1〇) in which R 2 to 4 in formula (4) selects a hydrogen atom: [Chem. 18]

(1〇) 〇 本發明之聚酯酿亞胺前驅物,其特徵在於:具有以下述 式(11)及式(12)所表示之重複單元,式(n)及式(12)之莫耳 比為式(11)/式(12)=20/80〜80/20之比例: [化 19](1〇) The polyester-bromide precursor of the present invention, which has a repeating unit represented by the following formulas (11) and (12), and a moie of the formula (n) and the formula (12) The ratio of the formula (11) / formula (12) = 20 / 80 ~ 80 / 20: [Chem. 19]

(Π)(Π)

ArAr

ύ rH (12) 134489.doc -14- 200948862 (式(11)及式(12)中,Ar為以式(2)所表示之4價芳香族 基;式(12)中,丑2為選自式(13)至式(17)中之至少一種之2 價芳香族基: [化 20] (2) [化 21]ύ rH (12) 134489.doc -14- 200948862 (In the formulas (11) and (12), Ar is a tetravalent aromatic group represented by the formula (2); in the formula (12), ugly 2 is selected a divalent aromatic group of at least one of the formula (13) to the formula (17): [Chem. 20] (2) [Chem. 21]

[化 23][Chem. 23]

❹ (13) (14) (15)❹ (13) (14) (15)

134489.doc -15- (16) 200948862 [化 25]134489.doc -15- (16) 200948862 [Chem. 25]

(17) ;R1Q〜Ru表示碳數i〜6之烷基、氫原子,該等為分別獨 立,可相同亦可不同)。 於本發明之聚酯醯亞胺前驅物中,上述聚酯醯亞胺前驅 物中’式(12)中之β2較好的是以式(16)、式(17)或式⑴)所 表示之重複單元,進而較好的是以式〇6)所表示之重複單 元: [化 26] (18) 於本發明之聚酯醯亞胺前驅物中,其重量平均分子量 Mw較好的是3萬以上、40萬以下。 於本發明之聚酯醯亞胺前驅物中,獲得該聚酯醯亞胺前 驅物時所使用之以式(19)所表示之含有酯基之四甲酸二 酐,其特徵在於:將示差掃描熱量計(DSC)所顯示之熔解 熱峰值溫度設為(a)°C、將開始朝向熔解熱波峰上升的溫度 與波峰斜度保持恆定的溫度作為連接點之切線的交點之溫 度設為(brc,且設定溫度寬時,滿足(a)g 322°C 以及 5°C ·· 134489.doc -16 - 200948862 [化 27](17); R1Q to Ru represent an alkyl group having a carbon number of i to 6 and a hydrogen atom, and these may be independently and may be the same or different). In the polyester quinone imine precursor of the present invention, β2 in the formula (12) in the above polyester quinone imine precursor is preferably represented by the formula (16), the formula (17) or the formula (1)). The repeating unit is further preferably a repeating unit represented by the formula: 6): (18) In the polyester quinone imine precursor of the present invention, the weight average molecular weight Mw is preferably 3 More than 10,000, less than 400,000. In the polyester quinone imine precursor of the present invention, the ester group-containing tetracarboxylic dianhydride represented by the formula (19) used in obtaining the polyester quinone imine precursor is characterized in that a differential scanning is performed. The calorific value of the heat of fusion shown by the calorimeter (DSC) is (a) ° C, and the temperature at which the temperature toward the peak of the melting heat wave and the peak of the peak are kept constant as the intersection of the tangent to the joint point is set to (brc) And when the set temperature is wide, it satisfies (a)g 322 ° C and 5 ° C ·· 134489.doc -16 - 200948862 [化27]

本發明之聚酯醯亞胺’其特徵在於:其係使上述聚酯醯 亞胺前驅物醯亞胺化而獲得者。 本發明之聚酯醯亞胺之製造方法,其特徵在於:其係將 上述聚酯酿亞胺前驅物加熱或者使用脫水試劑使其酿亞胺 ▲ 化,而獲得聚酯醯亞胺者。 本發明之積層板’其特徵在於:其具有聚酯醯亞胺層與 金屬層’該聚醋酿亞胺層係由上述聚醋醯亞胺所構成者。 本發明之積層板’其特徵在於:其係藉由將聚酯醯亞胺 前驅物塗布於金屬、冶上,乾燥後將其加熱或者使用脫水試 劑使其醯亞胺化而獲得者。 本發明之可挽性印刷配線板,其特徵在於:其係以配線 將上述積層板之金屬層進行圖案化而成者。 [發明之效果] 由本發明之聚酯醯亞胺前驅物所獲得之聚酯醯亞胺,具 有兼具高阻燃性、低吸濕膨脹係數、與銅箔同等的低線熱 膨脹係數、尚玻璃轉移溫度、高接著性、低彈性率、高撕 裂強度之效果。 【實施方式】 作為用以使聚醯亞胺低線熱膨脹化之分子設計,必須儘 可能地使主鏈骨架成直線狀且具有剛性(難以藉由内部旋 轉而取得多種構形(conformati〇n))。然而,另一方面因 134489.doc 200948862 此會有聚合物鏈的糾纏減少且膜變脆弱之虞。又,向聚醢 亞胺骨架中過多地導入醚結構等彎曲性單元,可較大程度 地有助於膜勒性的提昇或與金屬箔的接著強度的提昇,但 推測會妨礙低線熱膨脹特性的表現。The polyester quinone imine of the present invention is characterized in that it is obtained by imidating the above polyester quinone precursor quinone. The method for producing a polyester quinone imine according to the present invention is characterized in that the polyester acrylonitrile precursor is heated or a dehydrating reagent is used to make an imine oxime to obtain a polyester quinone. The laminated board of the present invention is characterized in that it has a polyester quinone imine layer and a metal layer. The polyacetal layer is composed of the above-mentioned polyacetamide. The laminated board of the present invention is characterized in that it is obtained by applying a polyesterimide precursor to a metal, smelting, drying it, heating it, or imidating the hydrazine using a dehydrating agent. The switchable printed wiring board of the present invention is characterized in that the metal layer of the laminated board is patterned by wiring. [Effect of the Invention] The polyester quinone imine obtained from the polyester quinone imine precursor of the present invention has a high flame retardancy, a low hygroscopic expansion coefficient, a low linear thermal expansion coefficient equivalent to that of a copper foil, and a glass. The effect of transfer temperature, high adhesion, low modulus of elasticity, and high tear strength. [Embodiment] As a molecular design for thermally expanding a polyimine at a low line, it is necessary to make the main chain skeleton linear and rigid as much as possible (it is difficult to obtain various configurations by internal rotation) (conformati〇n) ). However, on the other hand, due to 134489.doc 200948862, there is a entanglement of the polymer chain and the film becomes weak. Further, excessive introduction of a flexible unit such as an ether structure into the polyimine skeleton can contribute to a large improvement in film affinity or an increase in adhesion strength to a metal foil, but it is presumed to hinder low-line thermal expansion characteristics. Performance.

於本發明中所關注之酯結構與醚結構相比,内部旋轉障 礙較间,構形變化相對地受到更多妨礙,因此可期待其發 揮作為剛性結構單元的作用,並且亦賦予聚醯亞胺主鏈以 一疋程度的柔軟度,從而提供可撓性膜。 又,因酯結構與醯胺結構或醯亞胺結構相比極化率較 低’故向聚醢亞胺中導入醋結構亦有利於降低吸濕膨脹係 數0 1發明中’可藉由選定具有特^的芳香族骨架及輯結 構單體作為酸一酐及二胺,向聚酿亞胺中導入特定的芳 香族骨架及㈣構,而獲得具有以下述式⑴所表示的重複 皁疋之聚酿醯亞胺前驅物。藉此,本發明之聚醋醯亞胺前 驅物可同時實現高阻燃性、低吸濕膨脹係數、與銅箔同等 的低線熱膨脹係數、高玻璃轉移溫度、高接著性、低彈性 率、以及高撕裂強度: [化 28] 0) .Ύ V _The ester structure of interest in the present invention is more resistant to internal rotation than the ether structure, and the configuration change is relatively more hindered, so that it can be expected to function as a rigid structural unit and also impart polyimine. The main chain provides a flexible film with a degree of softness. Moreover, since the ester structure has a lower polarizability than the guanamine structure or the quinone imine structure, the introduction of the vinegar structure into the polyimine is also advantageous for reducing the hygroscopic expansion coefficient. The aromatic skeleton and the monovalent monomer are introduced into a polyaromatic imine into a specific aromatic skeleton and a (tetra) structure to obtain a polysiloxane having a repeating saponin represented by the following formula (1). Brewed imine precursors. Thereby, the polyacetal imide precursor of the present invention can simultaneously achieve high flame retardancy, low moisture absorption expansion coefficient, low linear thermal expansion coefficient equivalent to copper foil, high glass transition temperature, high adhesion, low modulus of elasticity, And high tear strength: [Chem. 28] 0) .Ύ V _

Bj為選自 = (1)中’ Ar為以式(2)所表示之4價芳香為 〜式(9)中之至少一種之2價芳香族基: 134489.doc (2) 200948862 [化 29] [化 30]Bj is a divalent aromatic group selected from = (1) where 'Ar is a tetravalent aromatic represented by the formula (2) and is at least one of the formula (9): 134489.doc (2) 200948862 [Chemical 29 ] [Chem. 30]

[化 31][化31]

(3)(3)

(4) [化 32](4) [Chem. 32]

(5)(5)

[化 33][化33]

⑹ [化 34](6) [34]

⑺ 134489.doc •19- (8) 200948862 [化 35](7) 134489.doc •19- (8) 200948862 [Chem. 35]

[化 36][化36]

;Ri表示碳數1〜6之烷基;R2~R4表示碳數1〜6之烷基、氩 φ 原子’該等為分別獨立,可相同亦可不同;R5表示碳數 1〜6之烷基;尺6〜尺9表示碳數1〜6之烷基、氫原子。 本發明之聚酯酿亞胺前驅物’係藉由使用含有酯基之四 羧酸二酐單體以及含有酯基之二胺單體而製造。一般認為 根據二胺與酸二酐的反應位置有4種異構物,但醯亞胺化 後可由4種異構物可獲得相同的產物’因此所得聚醋酿亞 胺前驅物係以通式(1)來表示。 使本發明之聚酯醯亞胺前驅物聚合時,使用作為具有醋 © 基的單體之以式(19)所表示之具有酯結構之四羧酸二酐(以 下稱為TABP)作為必要成分,使用選自式(26)〜式(33)中之 至少一種二胺。&amp;表示碳數1〜6之烷基。〜1表示碳數 1〜6之烷基、氫原子,該等為分別獨立,可相同亦可不 同。R5表示碳數1〜6之烷基。〜表示碳數丨〜6之烷基、 氫原子。此處,就低彈性率、接著性之觀點而言,較好的 是式(26)、式(27),進而較好的是式(27),尤其好的是 (33): 134489.doc •20- (19)。 200948862 [化 37];Ri represents an alkyl group having 1 to 6 carbon atoms; R2 to R4 represents an alkyl group having 1 to 6 carbon atoms, and an argon φ atom' is independently independent and may be the same or different; R5 represents an alkyl group having 1 to 6 carbon atoms; Base; ruler 6 to rule 9 represents an alkyl group having 1 to 6 carbon atoms and a hydrogen atom. The polyester-bromide precursor of the present invention is produced by using a tetracarboxylic dianhydride monomer containing an ester group and a diamine monomer containing an ester group. It is generally believed that there are four isomers depending on the reaction position of the diamine and the acid dianhydride, but the same product can be obtained from the four isomers after the imidization of the hydrazine. Thus, the obtained polyacetal precursor precursor system has the general formula (1) to indicate. When the polyester quinone imine precursor of the present invention is polymerized, a tetracarboxylic dianhydride (hereinafter referred to as TABP) having an ester structure represented by the formula (19) as a monomer having a vinegar group is used as an essential component. At least one diamine selected from the group consisting of the formulae (26) to (33) is used. &amp; represents an alkyl group having 1 to 6 carbon atoms. ~1 represents an alkyl group having 1 to 6 carbon atoms and a hydrogen atom, and these are independently independent and may be the same or different. R5 represents an alkyl group having 1 to 6 carbon atoms. 〜 represents an alkyl group having a carbon number of 66 and a hydrogen atom. Here, from the viewpoint of low modulus of elasticity and adhesion, it is preferred that the formula (26), the formula (27), and further preferably the formula (27), particularly preferably (33): 134489.doc • 20- (19). 200948862 [化37]

[化 38][化38]

[化 40] (26) (27)[40] (26) (27)

[化 43] (28) (29) (30)[化43] (28) (29) (30)

( 3 1 134489.doc -21 - 200948862 [化 44] [化 45] (3 2 ) (3 3 ) Ο( 3 1 134489.doc -21 - 200948862 [化 44] [化 45] (3 2 ) (3 3 ) Ο

進而’就固化後積層板的翹曲、所得聚酯酿亞胺膜的撕 裂強度之觀點而言,使本發明之聚酯醯亞胺前驅物聚合 時’較好的是使用ΤΑΒΡ及以式(33)所表示之具有酯結構之 二胺(以下稱為ΒΡΙΡ)作為必要成分’進而使用選自式(34)〜 式(3 9)中之至少一種二胺;又,進而較好的是式(37)、式 (38)、式(39);就所得聚酯醯亞胺膜的撕裂強度之觀點而 吕’尤其好的是式(37): [化 46]Further, from the viewpoint of warpage of the laminated sheet after curing and tear strength of the obtained polyester-imide film, when the polyester quinone imine precursor of the present invention is polymerized, it is preferable to use hydrazine and (33) a diamine having an ester structure (hereinafter referred to as hydrazine) as an essential component, and further using at least one diamine selected from the group consisting of the formula (34) to the formula (39); further preferably Formula (37), formula (38), and formula (39); from the viewpoint of the tear strength of the obtained polyester quinone film, L' is particularly preferable to the formula (37): [Chem. 46]

(34) (35) [化 48](34) (35) [Chem. 48]

(36) 134489.doc -22- 200948862 [化 49](36) 134489.doc -22- 200948862 [Chem. 49]

[化 50] [化 51][化 50] [化 51]

;此處’ R1G〜Rls表示碳數1〜6之烷基、氫原子,該等為分 別獨立,可相同亦可不同。 已知有’一般而言具有與銅箔同等的線熱膨脹係數之聚 S曰酿亞胺膜在固化後其魅曲量較小,但已獲得不能一概地 僅以線熱膨脹係數來判斷固化後的翹曲之見解,具有與銅Here, R1G to Rls represent an alkyl group having 1 to 6 carbon atoms and a hydrogen atom, and these are independently independent and may be the same or different. It is known that a poly-stained imine film having a linear thermal expansion coefficient equivalent to that of a copper foil generally has a small amount of enchantment after curing, but it has been found that it cannot be judged only by linear thermal expansion coefficient. Warped insight, with copper

箔同等的線熱膨脹係數並且翹曲量較小者更適於Fpc基板 之加工步驟。 此處’為了將莫耳比設為通式(11)/通式(12)=2〇/8〇〜 80/20之比例,而將TABP與總二胺以大約1 :丨之比率加以 混合’將總二胺當作1〇〇 m〇l〇/。時,使用二胺莫耳數2〇 mol%〜80 mol%之BPIP,進而使用二胺莫耳數2〇 m〇m〜8〇 mol%之選自通式(34)〜通式(39)中之至少一種具有酯結構 之二胺。 此處,就線熱膨脹係數、固化後之積層板的翹曲、所獲 得膜的撕裂強度之觀點而言,該莫耳比較好的是通式〇1)/ 134489.doc •23· 200948862 通式(12)=20/80〜80/20之比例,更好的是通式(11)/通式 (12)=30/70-70/30之比例。 又,就製作無凝膠成分之咼分子量體之聚醯亞胺前驅物 /谷液、以及金屬/聚醯亞胺積層體的接著強度、聚醯亞胺 膜的撕裂強度之觀點而言,作為必要成分而使用之TABp 較好的是高純度者。具體而言,較好的是於由示差掃描熱 量計所顯示之圖1之曲線中,將熔解熱之峰值溫度設為(a) C,將以開始朝向熔解熱波峰上升的溫度作為連接點之假 β 設切線與沿熔解熱波峰的大致直線部分的直線之交點的溫 度設為(b)°c,且設定溫度寬△丁=(〇5)_(勾)£〇時,滿足(a)g 322 C及ΔΤ$ 5°C之TABP,進而較好的是滿足(a)g 325β(: 及 ΔΤ$ 4°C 之 TABP。 本發明者為了使TABP成為高純度者,而關注純化TABp 之過程’且發現下述情形。,本發明者發現:藉由以特 定的溶劑、《度、溫度條件進行再結曰曰曰,而有效地除去混 〇 合存在之以式(40)所表示之4,4,_雙酚衍生物、或推測是以 式(4D所表示之4,4i_雙酚與偏苯三酸酐醯氣發生開環反應 而獲得之募聚物等,其後藉由無水化加熱乾燥處理,而除 去結日日巾所R寸著的附著水及结晶水,從而將一部分再結晶 - 冑發生開環的四羧酸酸酐化’從而獲得高純度之ΤΑΒρ: [化 52] 134489.doc •24- (40) 200948862 [化 53]The equivalent thermal expansion coefficient of the foil and the smaller amount of warpage are more suitable for the processing steps of the Fpc substrate. Here, 'in order to set the molar ratio to the ratio of the general formula (11) / general formula (12) = 2 〇 / 8 〇 80 80 / 20, TABP and the total diamine are mixed at a ratio of about 1: 丨'To treat the total diamine as 1〇〇m〇l〇/. When using a diamine molar number of 2〇mol%~80 mol% of BPIP, and further using a diamine molar number of 2〇m〇m~8〇mol% selected from the general formula (34) to the general formula (39) At least one diamine having an ester structure. Here, in terms of the linear thermal expansion coefficient, the warpage of the laminated plate after curing, and the tear strength of the obtained film, the molar is preferably a formula 〇1) / 134489.doc • 23· 200948862 The ratio of the formula (12) = 20/80 to 80/20 is more preferably the ratio of the formula (11) / formula (12) = 30/70 to 70/30. Further, in view of the adhesion strength of the polyimine precursor/valley solution of the bismuth molecular weight body having no gel component and the metal/polyimine laminate, the tear strength of the polyimide film, The TABp used as an essential component is preferably a high purity one. Specifically, it is preferable that in the graph of FIG. 1 displayed by the differential scanning calorimeter, the peak temperature of the heat of fusion is (a) C, and the temperature at which the peak toward the melting heat wave starts is used as a connection point. False β sets the temperature at the intersection of the tangent line and the straight line along the substantially straight line portion of the melting heat peak as (b) °c, and satisfies (a) when the set temperature is wide Δ丁=(〇5)_(hook)〇 g 322 C and TABP of ΔΤ$ 5 °C, and further preferably TABP satisfying (a) g 325β (: and ΔΤ$ 4 ° C. The present inventors focused on purifying TABp in order to make TABP high purity. The process 'and found the following. The inventors found that by re-crusting with a specific solvent, "degree, temperature conditions, the effective removal of the mixed enthalpy is represented by the formula (40). 4,4,_bisphenol derivative, or a polymer obtained by a ring-opening reaction of 4,4i_bisphenol and trimellitic anhydride helium represented by the formula (4D), and then dried by anhydrous drying Processing, and removing the adhering water and crystal water of the R-day towel, thereby re-crystallizing a part of the crystallization - 胄 occurs The ring-opened tetracarboxylic anhydride is acidified to obtain a high purity ΤΑΒρ: [Chem. 52] 134489.doc •24- (40) 200948862 [Chem. 53]

- TABP伴隨純度的提高,由示差掃描熱量計(DSC)所顯示 之熔解熱波峰溫度向高溫側移動,並且將熔解熱波峰溫度 作為(a)°C、將以開始朝向熔解熱波峰上升的溫度作為連接 0 點之假設且線與沿熔解熱波峰之大致直線部分的直線之交 點的溫度作為(b)°C時,(a)與(b)之溫度差變小。 TABP可藉由以下方法而獲得:將藉由於有機溶劑中使 偏苯三曱酸酐醯氣與二醇反應或使酚類的低級烷酸酯與偏 苯三甲酸或其酸酐進行酯交換而獲得之反應產物,以特定 的溶劑、濃度、溫度條件進行再結晶,其後進行無水化加 熱乾燥處理。 作為用以獲得高純度TABP之再結晶中所使用之溶劑, ❹ 肖好的是具有環狀S旨結構之内S旨系溶劑、具有環狀嗣結構 或環狀碳酸酯結構或環狀砜結構之溶劑。例如可列舉:α_ =甲基-γ-戊内酯、α_亞甲基_γ_丁内酯、γ_亞甲基_丫_丁内 • 知戊内酯、γ_ 丁内酯、環戊酮、碳酸丙二脂、碳酸乙 :環丁砜。該等可單獨使用或者將2種以上混合使 +。該等之中’就溶解性、再結晶產率或經濟性之觀點而 。’較好的是使用丁内酯、γ_戊内酯、環丁颯。 則相:合劑之使用量’若考慮雜質之除去、再結晶產率, ,於1重量份之藉由反應所獲得之產物,為i重量份 I34489.doc •25· 200948862 〜1〇〇重量份。當將含有 的含有酯基之四甲酸二 固體成分濃度較好的是 的是20%以下。 〜150重量份,尤其好的是4重量份 酯基之四甲酸二酐與溶劑的溶液中 酐的濃度作為固體成分濃度時, 50%以下,就產率之觀點而言更好 進行再結晶時,以達到上述濃度之方式將含有醋基之四 甲酸—酐與特定量之溶劑混合’再將混合溶液加熱至150 c〜30(TC ’使其完全溶解。其後’藉由將該溶液放置至室 ❹- TABP with the increase in purity, the melting heat peak temperature indicated by the differential scanning calorimeter (DSC) moves to the high temperature side, and the melting heat peak temperature is taken as (a) ° C, which will start to rise toward the melting heat peak. The temperature difference between (a) and (b) becomes small when the temperature at the intersection of the line and the line along the line of the melting line of the melting heat peak is assumed to be (b) °C. TABP can be obtained by reacting phthalic anhydride helium with a diol in an organic solvent or transesterifying a lower alkanoate of a phenol with trimellitic acid or an anhydride thereof. The reaction product is recrystallized under specific solvent, concentration, and temperature conditions, and then subjected to anhydrous heating and drying treatment. As a solvent used for recrystallization in order to obtain high-purity TABP, it is preferable to have a cyclic S structure, a solvent, a cyclic fluorene structure or a cyclic carbonate structure or a cyclic sulfone structure. Solvent. For example, α_=methyl-γ-valerolactone, α-methylene_γ-butyrolactone, γ-methylene_丫_丁内· cis-lactone, γ-butyrolactone, cyclopentane Ketone, propylene carbonate, ethylene carbonate: sulfolane. These may be used alone or in combination of two or more. Among these, 'in terms of solubility, recrystallization yield or economy. Preferably, butyrolactone, γ-valerolactone, and cyclobutyl hydrazine are used. The phase: the amount of the mixture used 'If the impurity is removed, the recrystallization yield is taken, 1 part by weight of the product obtained by the reaction, i parts by weight I34489.doc •25·200948862~1〇〇 parts by weight . When the concentration of the solid content of the tetracarboxylic acid containing diester containing the ester group is preferably 20% or less. ~150 parts by weight, particularly preferably 4 parts by weight of the ester group, the concentration of the anhydride in the solution of the tetracarboxylic dianhydride and the solvent is 50% or less as the solid content concentration, and when recrystallization is better from the viewpoint of the yield Mixing the carboxylic acid-containing tetracarboxylic acid anhydride with a specific amount of solvent to achieve the above concentration', and heating the mixed solution to 150 c~30 (TC' to completely dissolve it. Thereafter) by placing the solution To the room

溫而獲得析出#,再過據析出物。藉由該步驟,使由反應 時所生成的以式(40)所表示之4 4,雙酚衍生物或以式㈠” 所表示之4’雙㈣推測係偏苯三甲酸酐酿氣發生開環反 應而獲得之寡聚物等殘存於濾、液巾,藉此可有效率地將其 除去: [化 54] (40) [化 55]Get the precipitation out of the temperature, and then the precipitation. By this step, the 4 4 bisphenol derivative represented by the formula (40) or the 4′ bis(tetra) represented by the formula (1)” generated by the reaction is opened to cause ring-opening of the trimellitic anhydride gas. The oligomer or the like obtained by the reaction remains in the filtration and liquid towel, whereby it can be removed efficiently: [54] (40)

(41) (此處’ η為1~5)。 於氮氣、氦氣、氬氣等惰性氣體環境中,於大氣壓或者 減壓下,以1°C/分〜2〇。〇/分之升溫速度,於2〇〇°c〜300°C之 溫度下’將藉由過濾而獲得的析出物進行3小時以上無水 化加熱處理’藉此除去附著於結晶上的附著水及結晶水, 134489.doc -26 - 200948862 且使一部分在再結晶時發生開環的四甲酸酸酐化。為了有 效率地除去附著於結晶中的附著水及結晶水,更好的是於 100C〜130C之溫度下保持30分鐘〜1小時後,於2〇〇°c〜300 C之溫度下進行3小時以上無水化加熱(脫水閉環反應)。 又,就均勻地加熱結晶物以避免結晶物局部變為高溫從而 發生去羧酸等分解反應之觀點而言,升溫速度較好的是2〇 °C /分以下。 由示差掃描熱量計(DSC)所顯示之熔解熱峰值溫度(a)〇c &amp; 係該物質之熔點(mp),自322〇c較好的是自325充起向高溫 側偏移,將開始朝向熔解熱波峰上升的溫度作為連接點之 假設切線與沿著熔解熱波峰的大致直線部分之直線之交點 的溫度設為(b)°C時,(a)與(b)之溫度差較好的是5〇c,溫度 差小於4°C與TABP的純度提高有關聯。藉由滿足該等條 件,能夠進行高分子量、無凝膠成分之聚酯醯亞胺前驅物 之聚合。 这又,為了獲得低吸濕膨脹係數,而不使用氟化單體(含 有氟原子之單體)等高價的單體,因而可低成本地製造兼 具上述特性之聚醯亞胺。 以下就本發明之實施形態加以詳細說明,但該等係本發 明之實施形態之一例’本發明並不限定於該等内容。 於本發明中可獲得一種具有以先前材料所無法獲得的物 性之材料,即如具有酯結構並且具有特定的芳香族結構之 單體的剛性、疏水性此類結構上的特徵以外,因較平衡地 加入適度的彎曲性,故在製成銅箔/聚酯醯亞胺之積層板 134489.doc •27· 200948862 以及聚酯醯亞胺膜時,兼具高阻燃性、低吸濕膨脹係數、 與銅箔同等的低線熱膨脹係數、高玻璃轉移溫度、可撓 性、高接著性、低彈性率以及高撕裂強度。 &lt;聚酯醯亞胺前驅物之製造方法&gt; 本發明之聚酯醯亞胺前驅物之製造方法並無特別限定, 可採用公知之方法。更具體而言,可藉由以下方法獲得。 首先將二胺溶解於反應溶劑,向其中緩慢地添加四羧酸 二酐粉末,使用機械攪拌器,於〇»c〜1〇〇〇c,較好的是2〇 °C~90°C下攪拌0.5小時〜100小時,較好的是1小時〜24小 時。此時’就聚合度之觀點及單體或所生成聚合物的溶解 性之觀點而言’單體濃度較好的是5質量%〜50質量%,進 而較好的是10質量。/。〜40質量%,尤其好的是10質量%〜25 質量%。可藉由在此單體濃度範圍内進行聚合,而獲得均 勾且具高聚合度之聚酯醯亞胺前驅物溶液。此處,所得聚 酯醯亞胺前驅物溶液與申請專利範圍中所記載之聚酯醯亞 胺則驅物係相同者。 聚酿酿亞胺膜之重量平均分子量(Mw)較好的是3萬〜4〇 萬’進而較好的是3萬〜30萬《又,尤其好的是5萬〜2〇萬。 此處,就韌性之觀點而言,較好的是3萬以上,進而較好 的是5萬以上。又,就接著性、塗布性之觀點而言,重量 平均刀子量(Mw)較好的是4〇萬以下’進而較好的是%萬以 下’尤其好的是20萬以下。 至於在不損及聚酯醯亞胺膜的要求特性以及聚酯醯亞胺 别驅物的聚合反應性之範圍内,可與TABp併用之芳香族 134489.doc -28- 200948862 四羧酸二酐,可列舉:3,3,,4,4,_聯苯四甲酸二酐、2,3,6,7_ 萘四甲酸二酐、均苯四甲酸二酐、3,3,,4,4,-二苯基酮四甲 酸二酐、3,3’,4,4'-聯苯醚四甲酸二酐、對伸苯基雙(偏苯三 曱酸單酯酸酐)、對甲基伸苯基雙(偏苯三甲酸單酯酸酐)、 3,3',4,4'-聯苯颯四曱酸二酐、2,2,_雙(3,4_二羧基苯基)六氟 丙酸一酐、2,2’-雙(3,4-二羧基苯基)丙酸二酐、^^萘 四甲酸二酐等。又,亦可併用該等中的2種以上。 至於在不損及聚酯醯亞胺膜的要求特性以及聚酯醯亞胺 前驅物的聚合反應性之範圍内能夠與TABp併用之脂肪族 四甲酸一酐,並無特別限定,可列舉:雙環[2 2·2]辛_7- 烯-2,3,5,6-四甲酸二酐、 5_(二氧雜四氫呋喃基_3_甲基 _3· 環己烯_1,2-二羧酸酐、4-(2,5-二氧雜四氫呋喃_3_基)·四氫 化萘-1,2-二缓酸酐、四氫呋喃_2,3,4,5-四甲酸二酐、雙環_ 3,3’,4,4’_四曱酸二酐、1,2,3,4-環丁烷四甲酸二酐、 1,2,3,4-環戊烷四曱酸二酐等。又,亦可併用該等中的2種 以上。 至於在不明顯損及本發明之聚酯醯亞胺前驅物的聚合反 應性、聚醋酿亞胺的要求特性之範圍内能夠與以通式 (26)〜通式(39)所表示之具有酯結構之二胺併用之芳香族二 胺’並無特別限定,可列舉:對苯二胺、間苯二胺、2,4-二胺基甲苯、2,5-二胺基甲苯、2,4-二胺基二甲苯、2,4_二 胺基四曱苯、4,4,-二胺基二苯基甲烷、4,4'-亞曱基雙(2-甲 基苯胺)、4,4,_亞甲基雙(2-乙基苯胺)、4,4'-亞甲基雙(2,6-二曱基苯胺)、4,4,·亞曱基雙(2,6-二乙基苯胺)、4,4,-二胺 134489.doc • 29- 200948862 基二苯醚、3,4,-二胺基二苯醚、3,3,-二胺基二苯醚、2,4,-二胺基二苯醚、4,4,-二胺基二苯颯、3,3,-二胺基二苯艰、 4,4^二胺基二苯基酮、3,3’-二胺基二苯基酮、4,4,-二胺基 苯曱醯苯胺、聯苯胺、3,3,-二羥基聯苯胺、3,3,-二甲氧基 聯苯胺、鄰聯甲苯胺、間聯甲苯胺、2,2'-雙(三氟甲基)聯 苯胺、1,4-雙(4-胺基苯氧基)苯、1,3-雙(4-胺基苯氧基) 苯、1,3-雙(3-胺基苯氧基)苯、4,4,-雙(4-胺基苯氧基)聯 苯、雙(4-(3-胺基苯氧基)苯基)颯、雙(4-(4-胺基苯氧基)笨 基)礙、2,2-雙(4-(4-胺基苯氧基)苯基)丙烷、2,2-雙(4-(4- 胺基苯氧基)苯基)六氟丙烷、2,2-雙(4-胺基苯基)六氟丙 烧、對三聯苯基二胺等。又,亦可併用該等中的2種以 上。 至於在不明顯損及本發明之聚酯醯亞胺前驅物的聚合反 應性、聚酯醯亞胺的要求特性之範圍内能夠與以通式 (26)〜通式(39)所表示之具有酯結構之二胺併用之脂肪族二 胺’並無特別限定,例如可列舉:4,4,_亞曱基雙(環己 胺)、異佛爾酮二胺、反式-1,4-二胺基環己烷、順式·Μ_ 二胺基環己烷、1,4-環己烷雙(甲基胺)、2,5-雙(胺基甲基) 雙環[2.2.1]庚烷、2,6_雙(胺基甲基)雙環[2 21]庚烷、3,8_ 雙(胺基甲基)三環[5.2.1.0]癸烷、丨,%二胺基金剛烷、22_ 雙(4-胺基環己基)丙烷、2,2_雙(4_胺基環己基)六氟丙烷、 1,3-丙院二胺、1&gt;4_四亞甲基二胺、1&gt;5_五亞甲基二胺、 1,6-六亞甲基二胺、17•七亞曱基二胺、18八亞曱基二 胺、丨,9·九亞甲基二胺。又’可併用該等中的2種以上。 134489.doc -30- 200948862 Ο ❹ 作為進行聚合反應時所使用之溶劑,只要可使原料單體 及所生成之㈣酿亞胺前驅物溶解則無問題 無特別限定》具嫌可列舉:一基甲酿胺、Ν;= 基乙醯胺、Ν·甲基吡咯啶酮等之胺系溶劑;丫_丁内酯、丫_ 戊内知、δ-戊内酯、γ_己内西旨、ε己内酯、甲基个丁内 S:等之環狀6旨系溶劑;碳酸乙二醋、碳酸丙二脂等之碳酸 自曰系冷劑,二乙二醇等之醇系溶劑;間甲酚、對甲酚、3· 氯苯酚、4-氣苯酚等之酚系溶劑;苯乙酮、丨,3 •二甲基 味嗤咬_、環丁硬、二甲基亞礙等。就溶解性之觀點而 言,較好的是Ν,Ν-二甲基甲酿胺、Ν,Ν_二甲基乙酿胺、ν_ 甲基_2_°叫_、二甲基亞硬、1,3-二甲基-2“米哇琳酮等 之非質子性極性溶劑。 又’亦可添加使用其他普通的有機溶劑 盼、乙酸丁醋、乙酸乙酿、乙酸異丁醋、丙二醇單甲= 酸酯、2-乙氧基乙醇、2_ 丁氧基乙醇、乙二醇甲醚乙酸 醋、乙二醇乙騎乙酸醋、乙二醇丁鰱乙酸酿、四氫咳喃、 二甲氧基乙烷、二乙氧基乙烷、二丁醚、二乙二醇二甲 鍵、甲基異丁基闕、二異丁基,、環己綱、甲基乙基鲷、 丙酮、丁醇、乙醇、二甲苯、甲苯、氣苯、松節油 (turpentine)、礦油精、石油精系溶劑等。 本發明之聚醋醯亞胺前驅物,亦可將其溶液滴加至大量 的水或甲醇以良溶财並進行過濾、乾燥,作為粉末加 以分離。 &lt; 聚酯醯亞胺之製造方法&gt; 134489.doc • 31 - 200948862 本發明之聚酯醯亞胺,可藉由將以上述方法所獲得之聚 酯醯亞胺前驅物進行脫水閉環反應(醯亞胺化反應)而製 造。此時’聚酯醯亞胺之可使用形態為膜、金屬箔/聚醋 醯亞胺之積層板、粉末、成形體以及溶液。 將聚酯醯亞胺前驅物溶液流延至銅箔、鋁ϋ等金屬馆 上,於烘箱中於40°C ~1 80°C、較好的是5〇°C〜150°C下進行 乾燥。使用膠帶將所獲得之金屬/聚酿醯亞胺前驅物之積 層板黏貼固定於SUS製金屬板上,於真空中、氮氣等惰性 氣體中、或者空氣中’於200°C ~430°C較好的是250°C〜400 °c下進行加熱,藉此獲得金屬/聚醯亞胺積層板。將該積 層板之金屬層#刻除去’藉此可製造本發明之聚酯酿亞胺 膜。又,亦存在使用蒸鑛有金屬之石夕基板而獲得聚酯醯亞 胺膜之方法。此時,使聚酯酿亞胺前驅物溶液流延至蒸鍍 有金屬層之矽基板上,以上述方法進行乾燥、加熱,而獲 得蒸鑛有金屬層之梦/聚酯醯亞胺層之積層板。其後,對 該積層體之金屬層進行蚀刻,自石夕基板上剝離聚酯醯亞胺 層(聚酯醯亞胺膜),藉此可獲得目標物。 又’進而亦存在使用玻璃基板而獲得聚酯醯亞胺膜之方 法。將聚酯醯亞胺前驅物溶液流延至玻璃基板上,於烘箱 中於40°C〜18(TC較好的是50°c〜15〇t下進行乾燥,獲得玻 璃基板/聚酯醯亞胺前驅物層之積層板。其後,自該積層 板上剝離聚酯醯亞胺前驅物層(聚酯醯亞胺前驅物膜),使 用膠帶將該聚酯醯亞胺前驅物膜固定於金屬框上,以上述 方法進行加熱,藉此可獲得聚酯醯亞胺膜。 134489.doc -32- 200948862 就酿亞胺化之閉環反應之觀點而言,反應溫度較好的是 200 °C以上,就所生成之聚酯醯亞胺膜之熱穩定性之觀點 而言,反應溫度較好的是43(TC以下。醯亞胺化較好的是 於真空中或者惰性氣體中進行,但若醯亞胺化溫度並不過 分高,則亦可於空氣中進行》 又,代替熱處理,醯亞胺化反應亦可藉由以下方法進 行:將吡啶或三乙胺等3級胺添加至聚酯醯亞胺前驅物溶 液中製作聚酯醯亞胺前驅物膜,一面於200 °C〜3 00 °C下加 熱一面進行化學醯亞胺化;或於吡啶或三乙胺等3級胺存 在下,將聚酯醯亞胺前骚物膜浸潰於含有乙酸酐等脫水試 劑之溶液中。 此處,就由聚酯醯亞胺前驅物溶液來製造聚酯醯亞胺膜 之方法加以說明,但並不限定於此方法,亦可藉由加熱或 者使用脫水試劑,使經加熱乾燥之聚酯醯亞胺前驅物膜或 經分離之聚酯醯亞胺前驅物發生環化反應等,而製造聚酯 醯亞胺。於聚酯醯亞胺不溶於溶劑之情形時,可獲得作為 沈澱物之結晶性聚酯醯亞胺粉末。將聚酯醯亞胺粉末於 200°C~450°C較好的是25(TC〜430°C下進行加熱壓縮,藉此 可製作聚酯醯亞胺之成形體。 又,向聚酯醯亞胺前驅物溶液中添加N,N'-二環己基碳 二醯亞胺或三氟乙酸酐等脫水試劑並加以攪拌,使其於〇 °C〜100°C較好的是0°C〜60°C下反應,藉此生成聚酯醯亞胺 之異構物即聚異醯亞胺(poly iso imide)。以與上述相同之程 序將聚異醯亞胺溶液進行製膜後,於250°C〜450。(:較好的 134489.doc •33· 200948862 是27(TC〜40(TC下進行熱處理,藉此可容易地將其變換成 聚酯醯亞胺。異醯亞胺化反應,亦可將聚酯醯亞胺前驅物 膜浸潰於上述含有脫水試劑之溶液中而進行。 於聚醋酿亞胺溶解於溶劑之情形時,直接將聚酿酿亞胺 前驅物溶液或者以相同溶劑將其適度稀釋後加熱至15〇&lt;^ 〜200°C,藉此可容易地製造聚酯醯亞胺溶液。此時,為了 共沸蒸餾除去醯亞胺化的副產物即水等,亦可添加甲苯或 二甲苯等。又,亦可添加γ-曱基叹啶等鹼作為觸媒。 亦可將所得聚酯醯亞胺溶液滴加至大量的水或甲醇等不 良溶劑中再進行過濾,而分離出作為粉末之聚酯醯亞胺。 又,可將聚酯醯亞胺粉末再溶解於上述溶劑中而形成聚酯 醯亞胺溶液。 本發明之聚酯醯亞胺係藉由將本發明之聚酯酿亞胺前驅 物醯亞胺化而獲得。通常,可藉由調節製造中之四甲酸二 酐與二胺化合物之投入比,而調節所生成聚酯醯亞胺之分 子量或末端結構。較佳的總四甲酸二酐與總二胺之莫耳比 為 0.90〜1 ·ΐ〇。 所得聚酯醯亞胺之末端結構,根據製造時總四曱酸二酐 與總二胺之莫耳投入比的不同,而成為胺或者酸酐結構。 於末端結構為胺之情形時,可利用羧酸酐來進行末端密 封。至於該等之例,可列舉:鄰苯二甲酸酐、4_苯基鄰笨 一甲酸if、4-苯氧基鄰苯三甲酸軒、4•苯基幾基鄰苯二甲 酸酐、4-苯基磺醯基鄰苯二甲酸酐等,但並不限定於該 等。可單獨使用該等羧酸酐,或者將2種以上混合使用。 134489.doc -34- 200948862 又,於末端結構為酸酐之情形時,可利用單胺類來進行 末端密封。具體可列舉:苯胺、曱苯胺、胺基酴、胺基聯 苯、胺基二苯基酮、萘胺等。可單獨使用該等單胺,或者 將2種以上混合使用。 關於加成聚合條件,可依照先前進行之聚胺酸之加成聚 合條件進行。具體而言,首先於氮氣、氦氣、氬氣等惰性 環境中,於大氣壓下於0°C〜80°C下使芳香族二胺類溶解於 溶劑中’於4〇。〇〜1〇〇。〇下一面迅速地添加四甲酸二酐一面 使其加成聚合4小時〜8小時。藉此獲得聚酯醯亞胺前驅 物0 將上述聚酯酿亞胺溶液塗布於基板上,於4(TC〜400。(:較 好的是10(TC〜30(TC下進行乾燥,藉此亦可形成聚酯醯亞 胺膜。 將聚酯醯亞胺前驅物溶液塗布於金屬箔例如銅羯上再進 行乾燥後,利用上述條件進行醯亞胺化,藉此可獲得FPC 基板之原板即金屬層與聚酯醯亞胺層之積層板(FCCL)。此 處’使用銅箔作為金屬箔,將聚酯醯亞胺前驅物溶液直接 塗布於該銅箔上,藉此可獲得由銅箔與聚酯醯亞胺層所構 成之無接著劑2層型積層板。相對於此,使用環氧系接著 劑或熱塑性聚醯亞胺作為接著劑將聚酯醯亞胺層與銅箔加 以貼附之3層、偽2層型,亦作為FCCL之構成而為業者所 知’但此時接著劑必須具有熱塑性,因此接著劑之構成單 元中必須含有彎曲成分,從而導致吸濕膨脹係數變高、玻 璃轉移溫度及耐熱性降低。因此,於3層、偽2層型之積層 134489.doc -35- 200948862 板中’因隔著熱塑性接著層’故必然導致高吸濕膨脹係 數、低玻璃轉移溫度、以及低耐熱性。另一方面因本發 明之聚ss酿亞胺具有高接著性,故可不隔著接著層而獲得 2層型之積層板,並且聚酯醯亞胺本身亦具有非熱塑性。 因此亦可同時兼具高玻璃轉移溫度、高耐熱性以及低吸 濕膨脹係數。 作為FPC基板之金屬箔’可使用各種金屬箔,但較好的 是鋁泊、銅箔、不鏽鋼箔,尤其好的是銅箔。亦可對該等 金屬4進行粗化處理、電鍍處理、鉻酸鹽處理(chr〇mate treatment)、鋁醇化物處理、鋁螯合物處理、矽烷偶合劑 處理等表面處理β 金屬箱之厚度並無特別限定,但較好的是35 μηι以下, 更好的是1 8 μιη以下。 FCCL例如可以如下之方式製造。 首先’使用刮刀塗布機或帶緣塗布機、凹板印刷塗布機 荨將聚酯醯亞胺前驅物溶液塗布於金屬箔上。其後,使其 乾燥而形成聚酯醯亞胺前驅物層(以下亦稱為「聚酯醯亞 胺前驅物膜」)。塗布厚度會受到聚酯醯亞胺前驅物溶液 之固體成分濃度的影響,於氮氣、氦氣、氬氣等惰性環境 中’於200。(:〜4〇〇。(:下對聚酯醯亞胺前驅物層進行熱醯亞 胺化,藉此可形成聚酯醢亞胺層。聚酯醯亞胺層之厚度為 1〇〇 μΠ1以下,較好的是50 μπι以下,更好的是30 μιη以下。 又’此處聚酯醯亞胺層與金屬箔之剝離強度較好的是 0.8 N/mm以上,進而較好的是丨〇 N/mm以上。翹曲量較好 134489.doc -36- 200948862 用三氯化鐵水溶 的是10 mm以下,進而較好的是3 以下。 於室溫或者5(TC以下之加熱條件下, 液(鶴見#達股份有限公司製造,40波美(baume,比重單 位三氣化鐵含量為37%以上)作為姓刻溶液對上述fccl 進行敍刻,藉此將積層板之金屬層餘刻成所需之電路狀, 藉此可製造無接著劑型可撓性印刷配線板。 ❻(41) (here, 'η is 1~5). In an inert gas atmosphere such as nitrogen, helium or argon, at 1 ° C / min to 2 Torr under atmospheric pressure or reduced pressure. The temperature increase rate of 〇/min is carried out at a temperature of 2 ° C to 300 ° C, and the precipitate obtained by filtration is subjected to an anhydrous heat treatment for 3 hours or more to remove the adhered water adhering to the crystal and Crystal water, 134489.doc -26 - 200948862 and a portion of the ring-opening tetracarboxylic acid anhydride formed upon recrystallization. In order to efficiently remove the adhering water and the crystal water adhering to the crystal, it is more preferably maintained at a temperature of 100 C to 130 C for 30 minutes to 1 hour, and then at a temperature of 2 ° C to 300 C for 3 hours. The above anhydrous heating (dehydration ring closure reaction). Further, from the viewpoint of uniformly heating the crystallized material to prevent the crystal from being locally heated to a high temperature to cause a decomposition reaction such as decarboxylation, the temperature increase rate is preferably 2 ° C / min or less. The melting heat peak temperature (a) 〇c & shown by the differential scanning calorimeter (DSC) is the melting point (mp) of the substance, preferably from 325 〇c to 405 from the 325 charge to the high temperature side, When the temperature at which the temperature toward the melting heat wave peak rises is taken as the intersection of the hypothetical tangent to the connecting point and the straight line along the substantially straight portion of the melting heat peak is (b) ° C, the temperature difference between (a) and (b) is Preferably, 5 〇 c, the temperature difference of less than 4 ° C is associated with an increase in the purity of TABP. By satisfying these conditions, polymerization of a high molecular weight, gel-free polyester quinone imine precursor can be carried out. Further, in order to obtain a low hygroscopic expansion coefficient without using a high-priced monomer such as a fluorinated monomer (a monomer containing a fluorine atom), a polyimine having the above characteristics can be produced at low cost. Hereinafter, the embodiments of the present invention will be described in detail, but these are examples of the embodiments of the present invention. The present invention is not limited to the above. In the present invention, a material having physical properties which cannot be obtained by a prior material, that is, a structural property such as rigidity and hydrophobicity of a monomer having an ester structure and having a specific aromatic structure, can be obtained. Adding moderate flexibility, it has high flame retardancy and low moisture absorption coefficient when it is made into laminate of 134489.doc •27· 200948862 and polyester yttrium imide. The low linear thermal expansion coefficient, high glass transition temperature, flexibility, high adhesion, low modulus of elasticity, and high tear strength equivalent to copper foil. &lt;Production Method of Polyester Iridium Imine Precursor&gt; The method for producing the polyester quinone imine precursor of the present invention is not particularly limited, and a known method can be employed. More specifically, it can be obtained by the following method. First, the diamine is dissolved in the reaction solvent, and the tetracarboxylic dianhydride powder is slowly added thereto, using a mechanical stirrer, at 〇»c~1〇〇〇c, preferably 2〇°C~90°C. The stirring is carried out for 0.5 hour to 100 hours, preferably 1 hour to 24 hours. In this case, the monomer concentration is preferably from 5% by mass to 50% by mass, and more preferably from 10% by mass, from the viewpoint of the degree of polymerization and the solubility of the monomer or the polymer to be produced. /. ~40% by mass, particularly preferably 10% by mass to 25% by mass. A polyester quinone imine precursor solution which is uniform and has a high degree of polymerization can be obtained by carrying out polymerization within this monomer concentration range. Here, the obtained polyester phthalimide precursor solution is the same as the polyester oxime imide described in the patent application. The weight average molecular weight (Mw) of the polystyrene film is preferably from 30,000 to 40,000, and more preferably from 30,000 to 300,000. Further, particularly preferably from 50,000 to 20,000. Here, from the viewpoint of toughness, it is preferably 30,000 or more, and more preferably 50,000 or more. Further, from the viewpoint of adhesion and applicability, the weight average knife amount (Mw) is preferably 40,000 or less, and more preferably less than 10,000, and particularly preferably 200,000 or less. As for the aromatic 134489.doc -28- 200948862 tetracarboxylic dianhydride which can be used together with TABp within the range which does not impair the required properties of the polyesterimide film and the polymerization reactivity of the polyester quinone imide. , may be mentioned: 3,3,,4,4,_biphenyltetracarboxylic dianhydride, 2,3,6,7-naphthalenetetracarboxylic dianhydride, pyromellitic dianhydride, 3,3,,4,4, -diphenyl ketone tetracarboxylic dianhydride, 3,3',4,4'-diphenyl ether tetracarboxylic dianhydride, p-phenylene bis(p-trimellitic acid monoester anhydride), p-methylphenylene Bis(trimellitic acid monoester anhydride), 3,3',4,4'-biphenylfluorene tetraphthalic acid dianhydride, 2,2,_bis(3,4-dicarboxyphenyl)hexafluoropropionic acid Monoanhydride, 2,2'-bis(3,4-dicarboxyphenyl)propionic acid dianhydride, naphthalene tetracarboxylic dianhydride, and the like. Further, two or more of these may be used in combination. The aliphatic tetracarboxylic acid monoanhydride which can be used in combination with TABp in a range which does not impair the required properties of the polyester quinone imine film and the polymerization reactivity of the polyester quinone imine precursor is not particularly limited, and examples thereof include a double ring. [2 2·2]octyl-7-ene-2,3,5,6-tetracarboxylic dianhydride, 5-(dioxotetrahydrofuranyl_3_methyl_3·cyclohexene-1,2-dicarboxylate Anhydride, 4-(2,5-dioxatetrahydrofuran-3-yl)-tetrahydronaphthalene-1,2- bis-anhydride, tetrahydrofuran-2,3,4,5-tetracarboxylic dianhydride, bicyclo _ 3, 3', 4, 4'-tetradecanoic dianhydride, 1,2,3,4-cyclobutanetetracarboxylic dianhydride, 1,2,3,4-cyclopentane tetraphthalic acid dianhydride, etc. Two or more of these may be used in combination. As far as the polymerization reactivity of the polyester quin The aromatic diamine used in combination with the diamine having an ester structure represented by the formula (39) is not particularly limited, and examples thereof include p-phenylenediamine, m-phenylenediamine, and 2,4-diaminotoluene. 2,5-Diaminotoluene, 2,4-diaminoxylene, 2,4-diaminotetraphenyl, 4,4,-diamine Methane, 4,4'-fluorenylene bis(2-methylaniline), 4,4,_methylenebis(2-ethylaniline), 4,4'-methylenebis (2,6 -dimercaptoaniline), 4,4,-indenylbis(2,6-diethylaniline), 4,4,-diamine 134489.doc • 29- 200948862 phenyldiphenyl ether, 3,4, -diaminodiphenyl ether, 3,3,-diaminodiphenyl ether, 2,4,-diaminodiphenyl ether, 4,4,-diaminodiphenyl hydrazine, 3,3,-di Aminobiphenyl, 4,4 diaminodiphenyl ketone, 3,3'-diaminodiphenyl ketone, 4,4,-diaminophenyl anilide, benzidine, 3,3 ,-dihydroxybenzidine, 3,3,-dimethoxybenzidine, o-toluidine, m-toluidine, 2,2'-bis(trifluoromethyl)benzidine, 1,4-double ( 4-aminophenoxy)benzene, 1,3-bis(4-aminophenoxy)benzene, 1,3-bis(3-aminophenoxy)benzene, 4,4,-bis (4 -aminophenoxy)biphenyl, bis(4-(3-aminophenoxy)phenyl)anthracene, bis(4-(4-aminophenoxy)phenyl), 2,2- Bis(4-(4-aminophenoxy)phenyl)propane, 2,2-bis(4-(4-aminophenoxy)phenyl)hexafluoropropane, 2,2-bis(4- amine Phenyl) hexafluoropropane, p-terphenyldiamine, etc. Further, two or more of these may be used in combination, and the polymerization reactivity of the polyester quinone imine precursor of the present invention is not significantly impaired. The aliphatic diamine which can be used in combination with the diamine having an ester structure represented by the general formulae (26) to (39) in the range of the desired properties of the polyester quinone is not particularly limited, and examples thereof include, for example, 4,4,_-indenyl bis(cyclohexylamine), isophorone diamine, trans-1,4-diaminocyclohexane, cis-indole-diaminocyclohexane, 1,4 - cyclohexane bis(methylamine), 2,5-bis(aminomethyl)bicyclo[2.2.1]heptane, 2,6-bis(aminomethyl)bicyclo[2 21]heptane, 3,8_ bis(aminomethyl)tricyclo[5.2.1.0]decane, hydrazine, % diamine, adamantane, 22_bis(4-aminocyclohexyl)propane, 2,2-bis(4-amine Hexafluoropropane, 1,3-propanol diamine, 1&gt;4_tetramethylenediamine, 1&gt;5_pentamethylenediamine, 1,6-hexamethylenediamine, 17•seven-decyldiamine, 18-octadecyldiamine, anthracene, 9·nonamethylenediamine. Further, two or more of these may be used in combination. 134489.doc -30- 200948862 Ο ❹ As a solvent to be used in the polymerization reaction, there is no problem if the raw material monomer and the produced (IV)-bromide precursor are dissolved, and there is no particular limitation. Ammine amine, hydrazine; = amine solvent such as acetalamine or hydrazine methylpyrrolidone; 丫-butyrolactone, 丫_ 戊内知, δ-valerolactone, γ_hexine Ε-caprolactone, methyl-butane S: a cyclic solvent such as a solvent; a carbonate-based refrigerant such as ethylene carbonate or propylene carbonate; an alcohol solvent such as diethylene glycol; Phenolic solvents such as cresol, p-cresol, 3· chlorophenol, 4- phenol, etc.; acetophenone, anthracene, 3 • dimethyl miso bite _, cyclobutyrate, dimethyl sulphate, and the like. From the viewpoint of solubility, ruthenium, dimethyl dimethyl amide, hydrazine, hydrazine dimethyl ethanoamine, ν_methyl _2 _ _, dimethyl arylene, 1 is preferred. , 3-dimethyl-2" aprotic polar solvent such as mowolinone. Also 'other common organic solvents can be added, butyl acetate, acetic acid, isobutyl acetonate, propylene glycol monomethyl = acid ester, 2-ethoxyethanol, 2-butoxyethanol, ethylene glycol methyl ether acetate, ethylene glycol acetate, ethylene glycol butyrate, tetrahydrogen, dimethoxy Ethane, diethoxyethane, dibutyl ether, diethylene glycol dimethyl bond, methyl isobutyl hydrazine, diisobutyl butyl, cyclohexyl, methyl ethyl hydrazine, acetone, butanol, Ethanol, xylene, toluene, gas benzene, turpentine, mineral spirits, petroleum essence solvent, etc. The polyacetate imine precursor of the present invention may also be added dropwise to a large amount of water or methanol. It is well-dissolved, filtered, dried, and separated as a powder. &lt;Method for producing polyester quinone imine&gt; 134489.doc • 31 - 200948862 Polyester quinone imine of the present invention It can be produced by subjecting the polyester quinone imine precursor obtained by the above method to a dehydration ring-closure reaction (oxime imidization reaction). At this time, the form of the polyester quinone imide can be used as a film or a metal foil/ a laminate of polyacetal imide, powder, a shaped body and a solution. The polyester phthalimide precursor solution is cast onto a metal pavilion such as copper foil or aluminum crucible in an oven at 40 ° C to 180 ° C, It is preferred to carry out drying at 5 ° C to 150 ° C. The obtained metal/polyimide precursor laminate is adhered to a metal plate made of SUS using a tape, and is inert in a vacuum or a nitrogen atmosphere. Heating in a gas or air at a temperature of from 200 ° C to 430 ° C, preferably from 250 ° C to 400 ° C, thereby obtaining a metal/polyimine laminate. The metal layer of the laminate is # The polyester-imide film of the present invention can be produced by the engraving. Further, there is also a method of obtaining a polyester bismuth imide film by using a metal-plated substrate of a metal ore. The precursor solution is cast onto a substrate on which a metal layer is evaporated, and dried and heated in the above manner to obtain The steamed ore has a metal layer dream/polyester phthalimide layer laminated plate. Thereafter, the metal layer of the laminated body is etched, and the polyester bismuth layer is peeled off from the shixi substrate (polyester yttrium imide film) Therefore, the target object can be obtained. Further, there is a method of obtaining a polyester phthalimide film using a glass substrate. The polyester phthalimide precursor solution is cast onto a glass substrate at 40 ° C in an oven. ~18 (TC is preferably dried at 50 ° c to 15 ° t to obtain a laminate of a glass substrate / polyester phthalimide precursor layer. Thereafter, the polyester bismuth imide precursor is stripped from the laminate. The polyester layer (polyester phthalimide precursor film) was fixed on a metal frame using a tape, and heated by the above method, whereby a polyester phthalimide film was obtained. 134489.doc -32- 200948862 From the viewpoint of the ring closure reaction of the imidization, the reaction temperature is preferably 200 ° C or more, from the viewpoint of the thermal stability of the produced polyester ruthenium film. The reaction temperature is preferably 43 (TC or less. The ruthenium imidization is preferably carried out in a vacuum or in an inert gas, but if the imidization temperature is not excessively high, it can also be carried out in the air. Instead of heat treatment, the ruthenium imidization reaction can also be carried out by adding a tertiary amine such as pyridine or triethylamine to a polyester phthalimide precursor solution to prepare a polyester phthalimide precursor film, one side at 200 The chemical oxime imidization is carried out while heating at a temperature of ° C to 3 00 ° C; or the polyester yttrium imide film is impregnated with a dehydrating reagent such as acetic anhydride in the presence of a tertiary amine such as pyridine or triethylamine. Here, a method of producing a polyester phthalimide film from a polyester quinone imine precursor solution will be described, but it is not limited thereto, and it may be heated or used as a dehydrating agent. Heat dried polyester yttrium imide precursor film or separated polyester yam The precursor is subjected to a cyclization reaction or the like to produce a polyester quinone imine. When the polyester quinone imine is insoluble in a solvent, a crystalline polyester quinone imine powder as a precipitate can be obtained. The powder is preferably subjected to heating and compression at 200 ° C to 450 ° C at 25 (TC to 430 ° C), whereby a molded body of polyester quinone imine can be produced. Further, in a polyester phthalimide precursor solution A dehydrating agent such as N,N'-dicyclohexylcarbodiimide or trifluoroacetic anhydride is added and stirred, and the reaction is carried out at a temperature of from 0 ° C to 100 ° C, preferably from 0 ° C to 60 ° C. Thereby, a polyisoimide which is an isomer of polyester quinone imine is produced, and a polyisocyanine solution is formed into a film in the same procedure as above, and is then heated at 250 ° C to 450 ° C. : preferably 134489.doc •33· 200948862 is 27 (TC~40 (heat treatment under TC, which can be easily converted into polyester quinone imine. Iso-imidization reaction, polyester The quinone imine precursor film is impregnated in the above solution containing the dehydrating agent. When the polyacetal is dissolved in the solvent, the poly-bromide is directly The solution may be appropriately diluted with the same solvent and then heated to 15 〇 to 200 ° C, whereby the polyester quinone solution can be easily produced. At this time, the acetaminin is removed for azeotropic distillation. The product may be water or the like, and may be added with toluene or xylene, etc. Further, a base such as γ-mercaptopurine may be added as a catalyst. The obtained polyester phthalimide solution may also be added dropwise to a large amount of water or methanol. Further, the solvent is further filtered to separate the polyester quinone imide as a powder. Further, the polyester quinone imine powder can be redissolved in the solvent to form a polyester quinone imine solution. The imine is obtained by imidating the polyester-bromide precursor of the present invention. Generally, the molecular weight or terminal structure of the resulting polyester quinone imine can be adjusted by adjusting the ratio of the input of the tetracarboxylic dianhydride to the diamine compound in the manufacture. Preferably, the molar ratio of total tetracarboxylic dianhydride to total diamine is 0.90 to 1 · ΐ〇. The terminal structure of the obtained polyester quinone is an amine or anhydride structure depending on the molar ratio of total tetradecanoic dianhydride to total diamine at the time of production. In the case where the terminal structure is an amine, the carboxylic acid anhydride can be used for terminal sealing. As such examples, phthalic anhydride, 4-phenylene o-formic acid if, 4-phenoxy phthalic acid, 4, phenyl phenyl phthalic anhydride, 4- Phenylsulfonyl phthalic anhydride or the like, but is not limited thereto. These carboxylic anhydrides may be used singly or in combination of two or more. 134489.doc -34- 200948862 Further, in the case where the terminal structure is an acid anhydride, a monoamine can be used for terminal sealing. Specific examples thereof include aniline, indolediamine, amine hydrazine, aminobiphenyl, aminodiphenyl ketone, and naphthylamine. These monoamines may be used singly or in combination of two or more. The addition polymerization conditions can be carried out in accordance with the addition polymerization conditions of the previously performed polyamic acid. Specifically, the aromatic diamine is first dissolved in a solvent at 0 ° C to 80 ° C under an inert atmosphere such as nitrogen, helium or argon. 〇~1〇〇. The tetracarboxylic acid dianhydride was rapidly added to the underside to carry out addition polymerization for 4 hours to 8 hours. Thereby, the polyester quinone imine precursor 0 is obtained. The polyester bis-imine solution is applied to the substrate at 4 (TC to 400. (: preferably 10 (TC~30 (drying under TC) A polyester bismuth imide film can also be formed. The polyester bismuth imide precursor solution is applied onto a metal foil such as copper ruthenium and dried, and then yttrium imidized under the above conditions, whereby the original plate of the FPC substrate can be obtained. a laminate of a metal layer and a polyesterimine layer (FCCL). Here, 'a copper foil is used as a metal foil, and a polyester phthalimide precursor solution is directly coated on the copper foil, whereby a copper foil can be obtained. A non-adhesive two-layer laminate formed of a polyester quinone layer. In contrast, a polyester bismuth layer and a copper foil are attached by using an epoxy-based adhesive or a thermoplastic polyimide. It is also known as the composition of FCCL, but it must be thermoplastic. Therefore, the constituent elements of the adhesive must contain a bending component, resulting in a high coefficient of hygroscopic expansion. , glass transition temperature and heat resistance are reduced. Therefore, in 3 layers, pseudo 2 Type of laminate 134489.doc -35- 200948862 In the board 'caused by the thermoplastic adhesive layer', it will inevitably lead to high hygroscopic expansion coefficient, low glass transition temperature, and low heat resistance. On the other hand, the polyss of the present invention The amine has high adhesion, so that a two-layer type laminate can be obtained without the interlayer, and the polyesterimine itself has non-thermoplasticity. Therefore, it can also have high glass transition temperature, high heat resistance and low suction. Wet expansion coefficient. Various metal foils can be used as the metal foil of the FPC board, but aluminum bobbin, copper foil, and stainless steel foil are preferable, and copper foil is especially preferable. These metal 4 can also be roughened, The thickness of the surface treatment β metal box such as electroplating treatment, chromate treatment, aluminum alcoholate treatment, aluminum chelate treatment, and decane coupling agent treatment is not particularly limited, but is preferably 35 μηι or less. More preferably, it is 1 8 μηη or less. FCCL can be produced, for example, in the following manner: First, a polyester bismuth imide precursor solution is applied by using a knife coater or a belt coater or a gravure coater. On the metal foil, it is then dried to form a polyester phthalimide precursor layer (hereinafter also referred to as "polyester phthalimide precursor film"). The coating thickness is affected by the polyester quinone imine precursor solution. The influence of the concentration of the solid component is in the inert environment such as nitrogen, helium or argon, at 200. (:~4〇〇. (:: the thermal imidization of the polyester ylide precursor layer, borrowing This can form a polyester quinone layer. The thickness of the polyester quinone layer is 1 〇〇μΠ1 or less, preferably 50 μπι or less, more preferably 30 μηη or less. The peel strength of the layer and the metal foil is preferably 0.8 N/mm or more, and more preferably 丨〇N/mm or more. The warpage amount is preferably 134489.doc -36- 200948862 It is 10 water-soluble with ferric chloride. It is less than mm, and more preferably 3 or less. At room temperature or under heating conditions of 5 (TC or less), the liquid (manufactured by Tsurumi #达股份有限公司, 40 Baume (the specific gravity unit has a content of 37% or more) is used as the surname solution to describe the above fccl. By engraving, the metal layer of the laminate is engraved into a desired circuit shape, whereby a non-adhesive type flexible printed wiring board can be manufactured.

又,此處聚醯亞胺膜之撕裂強度’於26μπι之聚醯亞胺 膜中較好的是50 mN以上,更好的是6〇 mN以上,尤其好 的是80 mN以上。彈性率較好的是4 〇 Gpa〜6 5 Gpa。吸濕 膨服係數較好的是7 ppm/% RH以下’線熱膨脹係數較好的 是16 PPm/°C〜25 ppm厂C,玻璃轉移溫度較好的是35〇〇ca 上0 於本發明之聚酯醯亞胺及其前驅物溶液中,根據需要可 添加氧化穩定劑、填充料、助黏劑、^夕炫偶合劑、感光 劑、光聚合起始劑以及敏化劑等添加物。 因本發明之聚酯醯亞胺具有高阻燃性、低吸濕膨脹係 數、與銅箔同等的低線熱膨脹係數、高玻璃轉移溫度、高 接著強度、低彈性率以及高撕裂強度,故可應用於各種電 子裝置中之電氣絕緣膜、可撓性印刷配線板、顯示器用基 板、電子紙用基板、太陽電池用基板等中,尤其可用作可 撓性印刷配線板用基材。 以下,利用實施例更具體地說明本發明,但本發明並不 限定於該等實施例。再者,以下例中之物性值係藉由下述 所示之方法進行測定。 134489.doc •37· 200948862 &lt;聚酯醯亞胺前驅物溶液&gt; 首先’將含有酯結構之二胺溶解於N_曱基_2_吡略咬酮 中,向其中緩慢添加含有酯結構之四羧酸二酐粉末,利用 機械攪拌器於80。(:之加熱條件下攪拌3〜5小時。此時,在 單體濃度為10質量%〜2〇質量%之單體濃度範圍内進行聚 合’藉此獲得均勻且具高聚合度之聚酯醯亞胺前驅物溶 液。 &lt;銅箔/聚酯醯亞胺積層板&gt; 將1 2 μιη厚之銅箔(日本電解股份有限公司:USLp •馆)以 粗化面側成為表面之方式靜置於金屬製塗布台上。將塗布 台之表面溫度設定為90°C,利用刮刀將上述所獲得之聚酯 酿亞胺前驅物溶液塗布於銅箔粗化面上。其後,於塗布台 上靜置30分鐘,進而於乾燥器中於i〇(rc下靜置3〇分鐘 後獲付無黏性之銅纟自/聚醋酿亞胺前驅物之積層板(聚醋 醯亞胺刖驅物層之厚度為47 μιη及24 μιη)。繼而,利用膠 帶將銅箔/聚酯醯亞胺前驅物之積層板黏貼固定於sus製金 屬板上,於氮氣環境中,於熱風乾燥器中,以5〇C/分之升 溫速度於150 °C下進行30分鐘醯亞胺化,於200。(:下進行1 小時醯亞胺化’於4〇〇。(:下進行1小時醯亞胺化。其後,除 去SUS製金屬板’獲得銅箔/聚酯醯亞胺之積層板。 &lt;聚酯醢亞胺膜&gt; 於室溫或者5(TC以下之加熱條件下,利用三氣化鐵溶液 (镇見曹達股份有限公司製造,40波美,三氣化鐵含量為 370/。以上)對上述所獲得之銅箔/聚酯醯亞胺之積層板之鋼 134489.doc -38 - 200948862 治進行蚀刻,藉此獲得膜厚為26 μιη及12 μηι之聚醋醯亞胺 臈。 &lt;重量平均分子量:Mw&gt; 使用精密天秤測定o.oi g之聚酯醯亞胺前驅物溶液,將 其溶解於10 g之展開溶劑中。展開溶劑係藉由將2.61 g之 溴化鋰(Aldrich公司製造)、5.88 g之磷酸水溶液(和光純藥 工業公司製造’純度為8 5%)溶解於1 L之二甲基甲酿胺(和 光純藥工業公司製造,液相層析用)製作而成。使該溶液 通過10 μιη之過濾器進行過濾。其後,利用將作為保護管 柱之TSK guard Column Super Η-Η(商品名,東曹達公司製 造)與作為分離管柱之TSK-GEL SUPER HM-H(商品名,東 曹達公司製造)2根管柱串聯連接之gpc(膠體滲透層析儀, 曰本分光公司製造),並利用上述展開溶劑,以〇 5 ml/分 之流速測定分子量。利用聚苯乙烯對分子量進行換算。 &lt;玻璃轉移溫度:Tg&gt; 使用島津製作所製造之熱機械分析裝置(TMA_5〇),藉由 熱機械分析,於負荷為5 g、升溫速度為1〇〇c/分、氮氣環 境中(流里20 ml/分)、溫度5〇°C〜450°C之範圍内,對寬度3 mm、長度18mm(夾盤間長度為15〇1111)、厚度26μιη之聚&quot;醋 酿亞胺膜之伸長度進行測定,根據所獲得曲線之反曲點求 得聚酯醯亞胺膜(26 μιη厚)之玻璃轉移溫度。 &lt;線熱膨脹係數:CTE&gt; 使用島津製作所製造之熱機械分析裝置(ΤΜΑ_5〇),藉由 熱機械分析’於負荷為5 g、升溫速度為贼/分、策氣環 134489.doc -39· 200948862 境中(流量20 ml/分)、溫度為50°C〜450°C之範圍内,對寬 度3 mm、長度18 mm(央_盤間長度為15 mm)、厚度26 μηι之 聚酯醢亞胺膜之伸長度進行測定,以50°C〜200°C範圍内之 膜伸長度之平均值,求得聚酯醯亞胺膜(26 μιη厚)之線熱 膨脹係數。 &lt;吸濕膨脹係數:CHE&gt; 使用優貝克(ULVAC)理工股份有限公司製造之熱機械分 Ο ❹ 析裝置(TM-9400)以及濕度環境調整裝置(HC-1),於23 C、負何5 g之條件下測定寬度3 mm、長度30 mm(夾盤間 長度為15 mm)、厚度26 μιη之聚酯醯亞胺膜在濕度自30〇/〇 RH變化為70% RH時之伸長度,以3〇% RH〜7〇% RH中之膜 之伸長度平均值,求得聚酯醯亞胺膜之吸濕膨脹係數。 &lt;阻燃性&gt; 將厚度為12 μηι之聚酯醯亞胺膜製成4〇片大小為2〇 ^以長 X5 cm寬之試驗片。將4〇片試驗片中的片於η它、相對 濕度50%之核i竟中放置48小㈣上 &lt;受理狀態&gt;,將剩餘的 片於舰度7gc下進行168小時老化後於溫度為m、 相對濕度為20%以下之兹極怒a 之乾燥器中冷卻4小時。分別使用聚 酉印醯亞胺骐各5片,以其 基於UL94VTM試驗之評價方法,於 23 C、相對濕度為 ^境巾,制燃燒性試驗進行 ,.^ ^ 此時評價中所使用之火焰為20 mm大 小之藍色火焰,鋼渣 秒。) 9 100 C至700°C之升溫時間為42.9 &lt;焊踢耐熱性評價&gt; 134489.doc 200948862 ❹ ❹ 將銅箔/聚酯醯亞胺之積層板切割成長3 cmx寬3 cm之大 小’利用遮蔽帶(masking tape)對中心部進行2.5 cmx2.5 cm 之遮蔽’於與上述相同之條件下,利用三氣化鐵溶液(鹤 見曹達股份有限公司製造,40波美,三氣化鐵含量為37% 以上)對鋼箔進行蝕刻,獲得試驗片。將所獲得試驗片於 乾燥器中於l〇5°C下放置1小時以上使其乾燥後,於設定為 3〇〇°C之焊錫浴中,以與銅箔側接觸之方式將試驗片於焊 錫浴表面靜置2分鐘,以目視評價於銅箔與聚酯醯亞胺膜 中有無鼓起、皺褶的發生等外觀變化,將未發現外觀變化 之情形作為良好的結果(〇)。 &lt;煮沸焊錫耐熱性評價&gt; '與焊錫耐熱性評價同樣之方式進行製作而獲得試驗 片,將純化水加入附有回流冷卻器之容器内以浸潰所獲得 試驗片’㈣〇t下靜置2小時。其後,將試驗片投入至常 溫純化水中,各取出一片試驗片,用紙巾擦去兩面的水 分。其後’於設定為·。C之焊錫浴令,以與銅箱側接觸 之方式將各試驗片靜置於焊踢浴表面2分鐘,卩目視 於銅_醋酿亞胺膜中是否有鼓起、敏稽的發 變化」將未發料觀變化之情形料良好的結果(〇)。 &lt;銅箔與聚酯醯亞胺層之接著強度&gt; ^試驗;^定法’係基於nsc647i規格而進行。 銅聚醋酿亞胺之積層板切割成長15 — 二=蔽帶對一中心部進行寬度3_之遮 與上述相同之條件下抑氯化鐵溶 134489.doc 200948862 所獲得試驗片於乾燥器中於1〇5&lt;t下放置H、時以上使其乾 燥後,用兩面膠帶將其固定於厚度3 mmiFR_4*板上。 將寬度為3 mm之導體自其與聚S旨醯亞胺膜之界面處剝離, 將其貼附於鋁製帶上作為抓取部分,而製作試樣。 將所獲得試樣固定於島津製作所製造之拉伸試驗機 (AUTOGRAPH AG-10KNI)上。固定時,為了確實地沿9〇。 方向進行剝離而安裝夾具,測定以約5〇 mm/分之速度進行 剝離50 mm時之負荷’且計算出每! cm之接著強度。 &lt;彈性率&gt; 使用OLIENTEC股份有限公司製造之尺丁匕^⑺型拉伸試 驗裝置,以試驗長度50 mm、試驗速度50 mm/分拉伸3 mm x50 mm之聚醯亞胺膜,彈性率係由聚酯醯亞胺膜的拉伸伸 長率在0.4%〜1.0。/。之間之應力斜度而算出。(於5〇 mm之樣 品在伸長至100 mm時發生斷裂之情形時,記作「拉伸斷裂 伸長率為100%」。) 〈褲形撕裂強度(trouser tear strength)〉 將聚醋醯亞胺膜切割成50 mmx 1 50 mm作為樣品,使用 OLIENTEC股份有限公司製造之RTG-1210型拉伸試驗裝置 (安裝相同公司製造之UR-5〇N-D型荷重元(load cell)),以 JIS K7 12 8 -1中所記載之方法,以5 0 mm/分之試驗速度進行 測定。 &lt;翹曲&gt; 將銅箔/聚醋醯亞胺之積層板切割成10 cmxl〇 cm之大 小,將其於23 °C、濕度50%之恆溫恆濕室中放置一日。其 134489.doc -42· 200948862 後’分別測定樣品的4個邊與設置面之距離,將所測定之 距離之平均值作為翹曲之值。此處,將朝向聚酯醯亞胺侧 捲曲之情形作為(+)之值。 &lt;熔解熱峰值溫度(a)〇c,溫度寬△T=((b)_(a))&lt;Jc&gt; 秤量5 mg左右之以式(19)所表示之具有酯結構之四羧酸 二酐(以下稱為TABP),將其置入附屬的鋁試樣容器内,蓋 . 上蓋子,將其捲曲而製作測定樣品: [化 56] ❹Further, the tear strength of the polyimide film is preferably 50 mN or more, more preferably 6 〇 mN or more, and particularly preferably 80 mN or more in the polyimide film of 26 μm. The elastic modulus is preferably 4 〇 Gpa~6 5 Gpa. The moisture absorption coefficient is preferably 7 ppm/% RH or less. The linear thermal expansion coefficient is preferably 16 PPm/°C~25 ppm, and the glass transition temperature is preferably 35〇〇ca. In the polyester quinone imine and its precursor solution, an additive such as an oxidative stabilizer, a filler, an adhesion promoter, a smectic coupling agent, a sensitizer, a photopolymerization initiator, and a sensitizer may be added as needed. The polyester quinone imine of the present invention has high flame retardancy, low hygroscopic expansion coefficient, low linear thermal expansion coefficient equivalent to copper foil, high glass transition temperature, high adhesion strength, low modulus of elasticity, and high tear strength. The electric insulating film, the flexible printed wiring board, the display substrate, the electronic paper substrate, the solar cell substrate, and the like in various electronic devices can be used as a substrate for a flexible printed wiring board. Hereinafter, the present invention will be specifically described by way of examples, but the present invention is not limited to the examples. Further, the physical property values in the following examples were measured by the methods shown below. 134489.doc •37· 200948862 &lt;polyester phthalimide precursor solution&gt; Firstly, the diamine containing an ester structure was dissolved in N_mercapto-2-pyrrolidone, and the ester-containing structure was slowly added thereto. The tetracarboxylic dianhydride powder was passed through a mechanical stirrer at 80. (: stirring under heating for 3 to 5 hours. At this time, polymerization is carried out in a monomer concentration range in which the monomer concentration is 10% by mass to 2% by mass, thereby obtaining a uniform and high polymerization degree polyester hydrazine. Imine precursor solution. &lt;Copper foil/polyester phthalimide laminated plate&gt; The copper foil of 1 2 μm thick (Nippon Electrolytic Co., Ltd.: USLp • Pavilion) was allowed to stand on the surface of the roughened surface. On the metal coating table, the surface temperature of the coating table was set to 90 ° C, and the polyester-imide precursor solution obtained above was applied onto the roughened surface of the copper foil by a doctor blade. Thereafter, on the coating table. After standing for 30 minutes, and then in a desiccator for 3 minutes after standing at rc, a non-adhesive copper ruthenium/polyacetate precursor film laminate (polyacetate yttrium imide) was obtained. The thickness of the layer is 47 μm and 24 μm. Then, the laminate of the copper foil/polyester ylide precursor is adhered to the metal plate of SUS by a tape, in a nitrogen atmosphere, in a hot air dryer. The yttrium imidization was carried out at 150 ° C for 30 minutes at a heating rate of 5 ° C / min, at 200 ° (: After 1 hour, the imidization was carried out at 4 Torr. (: 1 hour of hydrazine imidization was carried out. Thereafter, the SUS metal plate was removed to obtain a copper foil/polyester phthalimide laminated plate. &lt;Polyester醢imine film&gt; At room temperature or under heating conditions of 5 (TC or less, using a three-iron solution (manufactured by Zhenda Caoda Co., Ltd., 40 Baume, three-ironized iron content of 370/. or more) The above-obtained copper foil/polyester phthalimide laminate steel 134489.doc -38 - 200948862 is etched to obtain a polyacetal oxime having a film thickness of 26 μm and 12 μηι. Average molecular weight: Mw> The polyester yttrium imide precursor solution of o. oi g was measured using a precision balance, and dissolved in 10 g of a developing solvent. The solvent was developed by using 2.61 g of lithium bromide (manufactured by Aldrich Co., Ltd.). 5.88 g of an aqueous phosphoric acid solution (manufactured by Wako Pure Chemical Industries, Ltd., 'purity of 85%) was dissolved in 1 L of dimethyl ketoamine (manufactured by Wako Pure Chemical Industries, Ltd., liquid chromatography). The solution is filtered through a 10 μηη filter. Thereafter, the use will serve as a protective column. TSK guard column Super Η-Η (trade name, manufactured by Tosoh Soda Co., Ltd.) and GPC (colloid permeable layer) connected in series with TSK-GEL SUPER HM-H (trade name, manufactured by Tosoh Corporation) as a separation column The analyzer was used to produce a molecular weight at a flow rate of 〇5 ml/min using the developing solvent. The molecular weight was converted by polystyrene. &lt;Glass transfer temperature: Tg&gt; The heat produced by Shimadzu Corporation was used. Mechanical analysis device (TMA_5〇), by thermomechanical analysis, at a load of 5 g, a heating rate of 1 〇〇 c / min, a nitrogen atmosphere (flow of 20 ml / min), a temperature of 5 ° ° C ~ 450 ° Within the range of C, the elongation of the vinegar-coated imine film with a width of 3 mm, a length of 18 mm (the length between the chucks is 15〇1111), and a thickness of 26 μm is measured, and the inflection point of the obtained curve is obtained. Glass transition temperature of polyester yttrium imide film (26 μm thick). &lt;Line thermal expansion coefficient: CTE&gt; Using a thermomechanical analysis device (ΤΜΑ_5〇) manufactured by Shimadzu Corporation, by thermomechanical analysis, the load was 5 g, the heating rate was thief/min, and the gas ring 134489.doc -39· 200948862 In the environment (flow rate 20 ml / min), temperature in the range of 50 ° C ~ 450 ° C, for a width of 3 mm, length 18 mm (central _ disk length of 15 mm), thickness of 26 μηι polyester 醢The elongation of the imine film was measured, and the linear thermal expansion coefficient of the polyester bismuth imide film (26 μm thick) was determined by the average of the film elongations in the range of 50 ° C to 200 ° C. &lt;Moisture absorption coefficient: CHE&gt; Using a thermomechanical branching device (TM-9400) and a humidity environment adjusting device (HC-1) manufactured by ULVAC Technology Co., Ltd., at 23 C, Elongation of polyester yttrium imide film with a width of 3 mm, a length of 30 mm (with a length between chucks of 15 mm) and a thickness of 26 μm under the condition of 5 g, when the humidity changes from 30 〇/〇RH to 70% RH The hygroscopic expansion coefficient of the polyester yttrium imide film was determined by the average value of the elongation of the film in 3% by RH to 7〇% RH. &lt;Flame-retardant&gt; A polyester quinone imine film having a thickness of 12 μm was prepared into a test piece having a size of 2 〇 ^ and a length of X 5 cm. The sheet in the 4-inch test piece was placed on the η, the relative humidity of 50% of the core i was placed on 48 small (four) upper &lt;receiving state&gt;, and the remaining piece was subjected to aging for 168 hours at a ship degree of 7 gc at a temperature. It was cooled in a drier of m and a relative humidity of 20% or less for 4 hours. Five pieces of each of the polyimidine imines were used, and the flammability test was carried out according to the evaluation method of the UL94VTM test at 23 C and the relative humidity of the environment. ^^ The flame used in the evaluation at this time Blue flame of 20 mm size, steel slag seconds. The heating time of 9 100 C to 700 °C is 42.9 &lt;Evaluation of heat resistance of welding kick&gt; 134489.doc 200948862 ❹ 切割 The laminate of copper foil/polyester phthalimide is cut to a size of 3 cm x width 3 cm. Using a masking tape to shield the center portion by 2.5 cm x 2.5 cm. Under the same conditions as above, using a three-gas iron solution (manufactured by Tsurumi Soda Co., Ltd., 40 Bomei, three gas iron) The content of the steel foil was etched to obtain a test piece. The obtained test piece was allowed to stand in a desiccator at 100 ° C for 1 hour or more, and then dried, and then placed in a solder bath set at 3 ° C in a contact with the copper foil side. The surface of the solder bath was allowed to stand for 2 minutes, and the appearance change such as the occurrence of bulging or wrinkles in the copper foil and the polyester yttrium imide film was visually evaluated, and the appearance change was not observed as a good result (〇). &lt;Evaluation of Heat Resistance of Boiler Solder&gt; 'The test piece was produced in the same manner as the evaluation of the solder heat resistance, and the purified water was placed in a container equipped with a reflux cooler to impregnate the obtained test piece' (4) 下t Set for 2 hours. Thereafter, the test piece was placed in normal temperature purified water, and each piece of the test piece was taken out, and the water on both sides was wiped off with a paper towel. After that, it is set to ·. In the solder bath of C, the test pieces were placed on the surface of the soldering bath for 2 minutes in contact with the side of the copper box, and the _ _ 醋 酿 酿 酿 酿 是否 是否 是否 是否 是否 是否 」 」 」 」 」 」 A good result (〇) is expected in the case where the change is not observed. &lt;Bound strength of copper foil and polyester quinone layer&gt;^Test; ^ method was carried out based on the nsc647i specification. Copper polyacetate-based imide laminate cutting growth 15 - 2 = cover tape to a central portion width 3_ covered with the same conditions as above to inhibit ferric chloride 134489.doc 200948862 obtained test piece in a desiccator Place H at 1〇5&lt;t and dry it, then fix it on a 3 mmiFR_4* plate with double-sided tape. A conductor having a width of 3 mm was peeled off from the interface with the polythene imide film, and attached to an aluminum belt as a gripping portion to prepare a sample. The obtained sample was fixed on a tensile tester (AUTOGRAPH AG-10KNI) manufactured by Shimadzu Corporation. When it is fixed, in order to be surely along 9〇. The direction was peeled off and the jig was attached, and the load at the time of peeling 50 mm at a speed of about 5 〇 mm/min was measured and the calculation was performed every! The strength of the cm. &lt;elasticity&gt; A polyimine film of 3 mm x 50 mm was stretched with a test length of 50 mm and a test speed of 50 mm/min using a tens. 7^(7) tensile test apparatus manufactured by OLIENTEC Co., Ltd. The rate is from 0.4% to 1.0 by the tensile elongation of the polyesterimine film. /. Calculated between the stress gradients between them. (When a sample of 5 mm is broken when it is stretched to 100 mm, it is referred to as "tensile elongation at break is 100%".) <trouser tear strength> Polyacetate The amine film was cut into 50 mm x 1 50 mm samples, and the RTG-1210 tensile tester manufactured by OLIENTEC Co., Ltd. (installed with the UR-5〇ND type load cell manufactured by the same company) was used as JIS K7. The method described in 12 8 -1 was measured at a test speed of 50 mm/min. &lt;warp&gt; The laminate of copper foil/polyacetal imide was cut into a size of 10 cm x 10 cm, and it was placed in a constant temperature and humidity chamber at 23 ° C and a humidity of 50% for one day. After 134489.doc -42· 200948862, the distance between the four sides of the sample and the set surface was measured, and the average value of the measured distance was used as the value of warpage. Here, the case of curling toward the polyester quinone side is taken as the value of (+). &lt;heating peak temperature (a)〇c, temperature width ΔT=((b)_(a))&lt;Jc&gt; A tetracarboxylic acid having an ester structure represented by the formula (19) weighing about 5 mg A dianhydride (hereinafter referred to as TABP), which is placed in an attached aluminum sample container, covered with a lid, and crimped to prepare a measurement sample: [Chem. 56] ❹

(19) ;同樣地,將未秤量之料樣容器與蓋子捲曲,將其作為 標準物質。將標準物質與測定樣品置於附有示差掃描 計(獄-60,島津製作所股份有限公司製造)之加熱爐内、, 於升溫速度為HTC/分、N2環境下,在室溫〜35代之(19) Similarly, the unmeasured sample container and the lid were crimped and used as a standard material. The standard substance and the measurement sample were placed in a heating furnace equipped with a differential scanning meter (Prison-60, manufactured by Shimadzu Corporation) at a temperature increase rate of HTC/min, N2, at room temperature to 35 rpm.

内進行測I將溶解熱之夺值溫度作為⑷。C,將開始朝向 熔解熱波峰上升的溫度作為連接點之假設切線與沿炼解執 波峰的大致為直㈣分之直線之交點的溫度作為㈣,; 算溫度寬則⑻·⑷再者,㈣標 = 與熱流量之校正。 貝退订/ 皿度 (實施例1) (合成例1 )TABP之合成 於1 L1分離式現瓶 川moi之偏笨三甲酸 氣(東京化成股份有限公司製造彳冷&amp; 合解於100 ml之N,N_二甲 134489.doc -43· 200948862 基甲醯胺溶液中,於氮氣環境巾以冰浴將其冷卻至代。 其後,以溫度成為机以下之方式,用2小時以剛啊的 授拌速度,將5G ml之N,N_二甲基甲醢胺、5() mi^比咬中 溶解有4,4,_雙岐溶液滴加至燒瓶中,其後於室溫下授摔 6小時。若開始滴加則溶液變紅’隨著滴加結束有黃色沈 澱物生成。The internal measurement I takes the temperature of the heat of dissolution as (4). C, the temperature at which the temperature toward the melting heat wave peak rises is taken as the temperature at the intersection of the hypothetical tangent of the joint point and the straight line of the substantially straight (four) point along the refining wave peak as (4), and the temperature is wide (8)·(4) again, (4) Mark = correction with heat flow. Shell Unsubscribe/Dish (Example 1) (Synthesis Example 1) Synthesis of TABP in 1 L1 Separate-type bottle-shaped moi-based stupid tricarboxylic acid gas (made by Tokyo Chemical Industry Co., Ltd. 彳 Cold &amp; N, N_Dimethyl 134489.doc -43· 200948862 In the carbamide solution, it is cooled to the next generation in a nitrogen bath in an ice bath. Thereafter, the temperature becomes the machine below, and the time is 2 hours. Ah, the mixing speed, 5G ml of N, N-dimethylformamide, 5 () mi ^ than the bite dissolved 4,4, _ biguanide solution was added to the flask, and then at room temperature The drop is given for 6 hours. If the drop is started, the solution turns red. 'A yellow precipitate is formed as the drop is added.

❹ 繼而’過據析出物’用Ν,Ν·二甲基f醯胺將其清洗,進 而用水進行清洗,然後重複過滤2次,將濾取物乾燥,而 獲得含有TABP之黃白色結晶。其後,—面以真空乾燥器 進行減壓,-面以1()口分之升溫迷度於13代下加熱乾燥 2小時’獲得作為未.純化TABP之黃色結晶。 &lt;TABP之純化&gt; 於3〇〇 mi燒瓶中,將10 g之所獲得未純化ΤΑΒρ置入15〇 ml之7·-丁内酯溶液中,用油浴加熱至2〇〇&lt;5(:,用3〇分鐘一 面攪拌一面使其溶解。此時未發現不溶物。其後,停止油 浴加熱及攪拌,緩慢冷卻至室溫。 藉由放置至室溫,溶液緩慢地分離成2層同時有針狀黃 白色結晶析出。藉由過濾將析出物分離,一面用真空乾燥 器進行減壓—面以1G口分之升溫速度於13代下加熱^燥 2小時後,進而w1(rc/分之升溫速度於20〇1下加熱乾燥6 小時,一面保持真空度一面冷卻至室溫後,調整為大氣 壓,然後獲得目標物之高純度TABP黃色結晶。 、 利用示差掃描熱量計(DSC_60,島津製作所股份有限公 司製造)測定5 mg之所得TABP,結果如表2所示,熔解熱 134489.doc -44- 200948862 之峰值溫度(3)為325。(:,溫度寬厶丁=((13)-0))=3.2。(:。 &lt;聚醋酿亞胺前驅物之聚合、醯亞胺化及聚酯酿亞胺膜特 性評價&gt; 向 '經充分乾燥之附帶攪拌機之密閉反應容器中,加入 12.84 mmol之以式(33)所表示之具有酯結構之二胺(以下稱 為BPIP) ’再加入61 ml2N甲基_2吡咯啶酮,將溶液加溫 至80 C使其溶解。溶解後,向該溶液中緩慢加入13.38 mmol之上述所得之TABp粉末。藉由攪拌3〇分鐘,而使溶 液黏度急劇增加。進而攪拌4小時,而獲得具有以通式〇) 所表不之重複單元之透明、均勻且黏稠的聚酯醯亞胺前驅 物溶液《此處,式(1)中,&amp;為以式(1〇)所表示之2價芳香 族基: [化 57]继 Then, the precipitates were washed with hydrazine, dimethyl dimethyl decylamine, and washed with water, and then filtered twice, and the filtrate was dried to obtain yellow-white crystals containing TABP. Thereafter, the surface was decompressed with a vacuum drier, and the surface was heated and dried at a temperature of 1 () for 1 hour to obtain a yellow crystal which was not purified TABP. &lt;Purification of TABP&gt; In a 3 〇〇mi flask, 10 g of the obtained unpurified ΤΑΒρ was placed in 15 〇ml of 7·-butyrolactone solution, and heated to 2 〇〇&lt;5 with an oil bath. (:, it was dissolved while stirring for 3 minutes. At this time, no insoluble matter was found. Thereafter, the oil bath was stopped and stirred, and slowly cooled to room temperature. The solution was slowly separated into 2 by standing at room temperature. The layer was simultaneously precipitated with needle-like yellow-white crystals. The precipitates were separated by filtration, and decompressed by a vacuum dryer. The surface was heated at a heating rate of 1 G for 13 hours, and then dried for 2 hours, and then w1 (rc) / The temperature rise rate is heated and dried at 20 ° C for 6 hours, and after cooling to room temperature while maintaining the degree of vacuum, the pressure is adjusted to atmospheric pressure, and then the high purity TABP yellow crystal of the target is obtained. Using a differential scanning calorimeter (DSC_60, The product obtained by Shimadzu Corporation was measured for 5 mg of TABP. The results are shown in Table 2. The peak temperature (3) of the heat of fusion 134489.doc -44- 200948862 was 325. (:, temperature is 厶 = = (13 )-0)) = 3.2. (:. &lt;polymerization of polyacetate precursors Evaluation of properties of ruthenium iodide and polyester-coated imine film&gt; To a well-dried closed reaction vessel equipped with a stirrer, 12.84 mmol of a diamine having an ester structure represented by the formula (33) was added (hereinafter referred to as For BPIP)', add 61 ml of 2N methyl-2-pyrrolidone, and warm the solution to 80 C to dissolve. After dissolving, slowly add 13.38 mmol of the above-obtained TABp powder to the solution. Minute, and the viscosity of the solution is sharply increased. Further stirring for 4 hours, a transparent, uniform and viscous polyester phthalimide precursor solution having a repeating unit represented by the formula 获得) is obtained. And &amp; is a divalent aromatic group represented by the formula (1〇): [Chem. 57]

[化 58][化58]

[化 59][化59]

(10)。 該聚醋酿亞胺刚驅物溶夜gp使於室溫及2〇。〇 下放置 134489.doc •45· 200948862 月亦完全不會發生沈澱、凝膠化,從而顯示較高的溶液儲 存穩定性。 將12 0„!厚之銅箔(日本電解股份有限公司,USLp箔)以 粗化面側成為表面之方式靜置於金屬製塗布台上。將塗布 〇之表面溫度設定為90 C,利用刮刀將聚酯醯亞胺前驅物 '谷液塗布於銅箔粗化面上。其後,於塗布台上靜置30分 鐘,進而於乾燥器中於lOOt下靜置30分鐘後,獲得無黏 f生之鋼洎/聚酯醯亞胺前驅物之積層體(聚酯醯亞胺前驅物 層之厚度為47 μιη及24 μηι)。繼而,用膠帶將銅箔/聚酯醯 亞胺前驅物之積層體黏貼固定於sus製金屬板上,於氮氣 環境中,於熱風乾燥器中,以5〇C/分之升溫速度於15〇。〇 下進行30分鐘醯亞胺化,於2〇(rc下進行H、時醯亞胺化, 於400 C下進行1小時醯亞胺化。其後,除去sus製金屬 板,獲得無捲曲之銅箔/聚酯醯亞胺之積層板。於室溫或 者50 C以下之加熱條件下,利用三氣化鐵溶液(鹤見曹達 叔伤有限公司製造,40波美,三氣化鐵含量為3 7%以上)對 »亥銅嬙/聚酯醯亞胺積層板之銅箔進行蝕刻,藉此獲得膜 厚為26 μπι及12 μηι之淡茶色聚酯酿亞胺膜。(10). The polyester vinegar imide was flooded with gp at room temperature and 2 Torr. Placement under 〇 134489.doc •45· 200948862 Also no precipitation or gelation occurred at all, indicating a high solution storage stability. The 12 0 „! thick copper foil (Nippon Electrolytic Co., Ltd., USLp foil) was placed on the metal coating table with the roughened side as the surface. The surface temperature of the coated crucible was set to 90 C, using a doctor blade The polyester yttrium imide precursor gluten solution was applied to the roughened surface of the copper foil. Thereafter, it was allowed to stand on the coating table for 30 minutes, and further allowed to stand at 100 Torr in a drier for 30 minutes to obtain a non-viscous f. The laminate of the raw steel crucible/polyester phthalimide precursor (the thickness of the polyester bismuth imide precursor layer is 47 μηη and 24 μηι). Then, the copper foil/polyester phthalimide precursor is taped. The laminate is adhered to a metal plate of SUS, and is heated at a temperature of 5 〇C/min in a hot air dryer at a temperature of 15 Torr in a nitrogen atmosphere for 30 minutes. H and hydrazine imidization were carried out, and hydrazine imidization was carried out for 1 hour at 400 C. Thereafter, the metal plate of SUS was removed to obtain a laminated sheet of non-crimped copper foil/polyester yttrium. Or under heating conditions of 50 C or less, using a three-iron solution (manufactured by Tsurumi Soda Untrain Co., Ltd., 40 Bomei, A copper foil with a thickness of 26 μm and 12 μηι is obtained by etching a copper foil of a ruthenium ruthenium/polyaniline yttrium laminate with a thickness of 3 7% or more. .

該膜厚為26 μιη之聚酯醯亞胺臈經丨8〇。彎曲試驗並未斷 裂,從而顯示可撓性。該聚酯醯亞胺膜對N_甲基_2_吡咯 啶酮或二甲基乙醯胺等有機溶劑並不顯示溶解性。又經 由TMA測定,該聚酯醯亞胺膜顯示有22 ppm/〇c (5〇&lt;t至 2〇〇 C之間的平均值)之與銅箔同等之低線熱膨脹係數。測 定吸濕膨脹係數,結果為5.0 ppm/。/。RH(30% RH至 70% RH 134489.doc -46- 200948862 之間的平均值),顯示有極低之吸; 、 〜%服係數。評價膜厚 為12 μηι之聚酯醯亞胺臈之阻燃性, 知果顯不UL94VTM-0 之性能。X,顯示良好的焊錫耐熱性、煮彿谭錫财轨性。彈性率為5.1⑽較低’於2 —之聚醋酿亞胺臈中褲形撕 裂強度為62 mN係高撕裂強度。 (實施例2) ΟThe polyester bismuth iodide having a film thickness of 26 μm was passed through 〇8〇. The bending test did not break and showed flexibility. The polyester quinone imine film does not exhibit solubility in an organic solvent such as N-methyl-2-pyrrolidinone or dimethylacetamide. Further, as determined by TMA, the polyesterimide film showed a low coefficient of thermal expansion equivalent to that of copper foil of 22 ppm/〇c (average value between 5 Å &lt; t to 2 〇〇 C). The coefficient of hygroscopic expansion was measured and found to be 5.0 ppm/. /. RH (average between 30% RH and 70% RH 134489.doc -46- 200948862), showing very low absorption; , ~% service factor. The flame retardancy of the polyester bismuth iodide having a film thickness of 12 μηι was evaluated, and the performance of UL94VTM-0 was not known. X, showing good solder heat resistance, boiled Tanxi financial track. The elastic modulus is 5.1 (10) lower. The crepe tear strength of the vinegar-like imine oxime is 62 mN high tear strength. (Example 2) Ο

G 向經充分乾燥之附帶攪拌機之密閉反應容器中,加入 6.42 mmol之BPIP、6.42匪〇1之以式(37)所表示之具有醋 結構之二胺(以下稱為APAB),再加入61…之义甲基_2·吡 咯啶酮,將溶液加溫至8〇t使其溶解。溶解後,向該溶液 中緩慢加入13.3 8 mmol之實施例1中所獲得之TABp粉末。 藉由攪拌30分鐘,而使溶液黏度急劇增加。進而攪拌4小 時’而獲得具有以式(11)及式(12)所表示之重複單元,且 式(H)與式(12)之莫耳比為式之比例之透 明、均勻且黏稠的聚酯醯亞胺前驅物溶液。此處,式(12) 中’ B2為以式(16)所表示之2價芳香族基:[化 60] [化 61] 134489.doc ου •47- (12) 200948862 、人Δ人ΗΛ2,G To a well-dried closed reaction vessel with a blender, add 6.42 mmol of BPIP, 6.42 匪〇1 of the diamine (hereinafter referred to as APAB) represented by formula (37), and then add 61... The meaning of methyl 2 · pyrrolidone, the solution was warmed to 8 〇t to dissolve. After the dissolution, 13.3 8 mmol of the TABp powder obtained in Example 1 was slowly added to the solution. The viscosity of the solution was sharply increased by stirring for 30 minutes. Further stirring for 4 hours', a transparent, uniform and viscous polyg which has a repeating unit represented by the formula (11) and the formula (12) and a molar ratio of the formula (H) and the formula (12) to the formula is obtained. Ester imine precursor solution. Here, in the formula (12), 'B2 is a divalent aromatic group represented by the formula (16): [Chem. 60] [Chem. 61] 134489.doc ου • 47- (12) 200948862, human Δ人ΗΛ2,

ArAr

Lhy yh _ [化 62] (16)〇 依照實施例1中所記載之方法進行製犋、醯亞胺化,而 製作聚酯醯亞胺膜,同樣地進行物性評價。物性值示於表 1。除表1所示外,勉曲量為i mm,亦顯示良好的值。 (實施例3) 向經充分乾燥之附帶攪拌機之密閉反應容器中,加入 8.99 mm〇kBPIP、3.85顏〇1之八则,再加入。…之 N甲基2比略咬酮,將溶液加溫至&amp; 〇使其溶解。溶解 後向該/会液中緩慢加入13 ·38 mmol之實施例1中所獲得 之TABP °藉由授拌3 G分鐘’而使溶液黏度急劇增加。進 而授拌4小時,獲得具有以通式⑴)所表示之重複單元及以 通式(12)所表示之重複單元、且通式(11)及通式(12)之莫耳 比為通式(11)/通式(12)=7g/3()之比例之透明、均勻且黏稠 的聚醋醯亞胺前驅物溶液。此處,通式(12)中,&amp;為以式 (16)所表示之2價芳香族基。 依照實施例1中所記栽之方法進行製膜、醯亞胺化,而 134489.doc •48· 200948862 製作聚酯醯亞胺膜,同樣地進行物性評價。物性值示於表 1。除表1所示以外,翹曲量為10 rnm,亦顯示良好的值。 (實施例4) 向經充分乾燥之附帶攪拌機之密閉反應容器中,加入 6.88 mmol之BPIP、6,88 mmol之以式(38)所表示之具有胺 結構之二胺(以下稱為DAB A) ’再加入65 ml之N-甲基-2-0比 略啶酮,將溶液加溫至80t使其溶解。溶解後,向該溶液 中緩慢加入14.33 mmol之實施例1中所獲得之TABP粉末。 藉由攪拌3 0分鐘,而使溶液黏度急劇增加。進而授拌4小 時’而獲得具有以通式(11)所表示之重複單元及以通式 (12)所表示之重複單元、且通式(u)與通式(12)之莫耳比為 通式(Π)/通式(12)=50/50之比例之透明、均勻且黏稍的聚 酉旨酿亞胺前驅物溶液。此處,通式(12)中,b2為以式(17) 所表示之2價芳香芳香族基: [化 63] (38) [化 64] 分产 ⑼。 依照實施例1中所記載之方法進行製膜、醯亞胺化,而 製作聚酯醯亞胺膜,同樣地進行物性評價。物性值示於表 134489.doc -49· 200948862 1。除表1所示以外,翹曲量為lmm,亦顯示良好的值。 (實施例5) 向經充分乾燥之附帶攪拌機之密閉反應容器中,加入 9.63 mmol之BPIP、4.13 mmol之以式(39)所表示之具有胺Lhy yh _ (6) 醯 The oxime imidization was carried out according to the method described in Example 1, and a polyester quinone imine film was produced, and physical properties were evaluated in the same manner. The physical property values are shown in Table 1. Except as shown in Table 1, the amount of distortion is i mm, which also shows good values. (Example 3) To a sufficiently dried mixer vessel equipped with a stirrer, 8.99 mm of BPkBPIP and 3.85 of 3.81 加入1 were added, and then added. N-methyl 2 is slightly ketone, and the solution is warmed to &amp; 〇 to dissolve. After the dissolution, 13·38 mmol of the TABP ° obtained in Example 1 was slowly added to the solution to increase the viscosity of the solution sharply by mixing 3 G minutes. Further, the mixture is stirred for 4 hours to obtain a repeating unit represented by the formula (1)) and a repeating unit represented by the formula (12), and the molar ratio of the formula (11) and the formula (12) is a general formula. (11) / A transparent, uniform and viscous polyacetal imide precursor solution of the formula (12) = 7g / 3 (). Here, in the formula (12), &amp; is a divalent aromatic group represented by the formula (16). Film formation and oxime imidization were carried out in accordance with the method described in Example 1, and a polyester phthalimide film was produced by 134489.doc • 48· 200948862, and physical properties were evaluated in the same manner. The physical property values are shown in Table 1. Except as shown in Table 1, the amount of warpage was 10 rnm, which also showed a good value. (Example 4) To a sufficiently dried closed reaction vessel equipped with a stirrer, 6.88 mmol of BPIP and 6,88 mmol of a diamine having an amine structure represented by the formula (38) (hereinafter referred to as DAB A) was added. 'Additionally 65 ml of N-methyl-2-0 ridicone, the solution was warmed to 80 t to dissolve. After the dissolution, 14.33 mmol of the TABP powder obtained in Example 1 was slowly added to the solution. The viscosity of the solution was sharply increased by stirring for 30 minutes. Further, the mixture is stirred for 4 hours to obtain a repeating unit represented by the formula (11) and a repeating unit represented by the formula (12), and the molar ratio of the formula (u) to the formula (12) is A transparent, uniform and viscous polyimide precursor precursor solution of the formula (Π) / formula (12) = 50/50. Here, in the formula (12), b2 is a divalent aromatic aromatic group represented by the formula (17): [Chem. 63] (38) [Chem. 64] (9). Film formation and hydrazine imidization were carried out in accordance with the method described in Example 1, and a polyester phthalimide film was produced, and physical properties were evaluated in the same manner. The physical property values are shown in Table 134489.doc -49· 200948862 1. Except as shown in Table 1, the amount of warpage was 1 mm, which also showed a good value. (Example 5) To a sufficiently dried closed reaction vessel equipped with a stirrer, 9.63 mmol of BPIP and 4.13 mmol of an amine represented by the formula (39) were added.

結構之二胺(以下稱為BPTP),再加入71 ml2N•甲基·2-吡 咯啶酮,將溶液加溫至8(rc使其溶解。溶解後,向該溶液 中緩慢加入14.79 mmol之實施例丨中所獲得之TABp粉末。 藉由攪拌30分鐘,而使溶液黏度急劇增加。進而攪拌4小 時,而獲得具有以通式(11)所表示之重複單元及以通式 (12)所表示之重複單元、且通式(n)與通式(12)之莫耳比為 通式(11)/通式(12)==70/30之比例之透明、均勻且黏稠的聚 酯醯亞胺前驅物溶液。此處,通式(丨2)中,&amp;為以式(18) 所表示之2價芳香芳香族基: [化 65]The structure of the diamine (hereinafter referred to as BPTP), then add 71 ml of 2 N-methyl-2-pyrrolidone, and warm the solution to 8 (rc to dissolve it. After dissolution, slowly add 14.79 mmol to the solution. The TABp powder obtained in the example was stirred for 30 minutes to increase the viscosity of the solution sharply, and further stirred for 4 hours to obtain a repeating unit represented by the formula (11) and represented by the formula (12). a repeating unit, and the molar ratio of the general formula (n) to the general formula (12) is a transparent, uniform and viscous polyester yam of the formula (11) / general formula (12) == 70/30. An amine precursor solution. Here, in the formula (丨2), &amp; is a divalent aromatic aromatic group represented by the formula (18): [Chem. 65]

[化 66][化66]

(18) 依照實施例1中所記載之方法進行製膜、醯亞胺化,而 製作聚酯醯亞胺膜’同樣地進行物性評價。物性值示於表 1。除表1所不以外,翹曲量為-3 mm,亦顯示良好的值。 134489.doc -50- 200948862 此處,所謂-3 mm係指向銅箔側鲍曲之意思。 (實施例6) 向經充分乾燥之附帶攪拌機之密閉反應容器中加入5〇 mmol之BPIP,使其溶解於191 ml之N-甲基-2- °比洛咬酮 中’然後向該溶液中緩慢加入50 mm〇i之實施例i中所獲得 之TABP粉末。30分鐘後,溶液黏度急劇增加。進而於8〇 C下攪拌4小時,而獲得透明、均勻且黏稠的聚酯醯亞胺 刖驅物。所得聚6旨酿亞胺前驅物即使於室溫及_2〇下放 〇 置一個月亦完全不會發生沈澱、凝膠化,從而顯示較高的 洛液儲存穩疋性。於N -甲基-2 - °比略〇定嗣中,於3 〇、〇 5 質量%濃度下以奥士瓦黏度計(Ostwald's viscometer)所測 定之聚酯醯亞胺前驅物之固有黏度為2·8 dL/g。於氮氣3 kg/cm2之加壓條件下,將該聚酯醯亞胺前驅物以5 μιη薄膜 過渡器進行過遽,而獲得作為目標之聚g旨酿亞胺前驅物。 依照實施例1中所記載之方法進行製膜、醯亞胺化,藉 ◎ 此獲得膜厚為25 μιη及12 μηι之淡茶色聚酯醯亞胺膜,同樣 地進行物性評價。物性值示於表3。該聚酯醯亞胺膜即使 經180。彎曲試驗亦不會發生斷裂,從而顯示可撓性。又, 對任何有機溶劑均完全不顯示溶解性。 又’利用旋轉塗布機(MS-250 ’ Mikasa股份有限公司製 造)將上述所獲得之聚酯醯亞胺前驅物旋塗於6吋之砂晶圓 上,於乾燥器中於100°C下靜置30分鐘後,獲得無黏性的 聚酿酿亞胺前驅物/石夕晶圓積層體(聚酷酿亞胺前驅物層之 厚度為1 7 μπι)。其後’於氮氣環境中,於熱風乾燥器中, 134489.doc 200948862 以5°C/分之升溫速度,於i5〇°C下對積層體進行30分鐘酿 亞胺化、於200°C下進行I小時醢亞胺化、於400°C下進行j 小時酿亞胺化。其後’利用氫氟酸將聚酯酿亞胺膜自矽晶 圓上剝離’而獲得厚度為10 μιη之聚酯醯亞胺膜。對所獲 得之聚酯酿亞胺膜進行拉伸試驗,獲得彈性率為54 GPa 以及斷裂伸展率為53%之結果。 再者,此處’固有黏度(η)係於301:下利用舆士瓦黏度 計測定0.5質量%之聚酯醯亞胺前驅物而得。 ❹(18) The film properties and the oxime imidization were carried out in accordance with the method described in Example 1, and a polyester phthalimide film was produced. The physical property values are shown in Table 1. Except for Table 1, the amount of warpage was -3 mm, which also showed good values. 134489.doc -50- 200948862 Here, the term "-3 mm" refers to the side of the copper foil. (Example 6) 5 〇mmol of BPIP was added to a well-dried sealed reaction vessel equipped with a stirrer, and dissolved in 191 ml of N-methyl-2-° pirone, and then into the solution. The TABP powder obtained in Example i of 50 mm 〇i was slowly added. After 30 minutes, the viscosity of the solution increased sharply. Further, it was stirred at 8 ° C for 4 hours to obtain a transparent, uniform and viscous polyester quinone imide. The obtained poly(6) imine precursor was precipitated and gelled at room temperature and at _2 Torr for one month, indicating a high storage stability of the solution. In the N-methyl-2 - ° ratio, the intrinsic viscosity of the polyester quinone imine precursor measured by the Ostwald's viscometer at 3 〇 and 〇 5 mass % is 2 · 8 dL/g. The polyester quinone imine precursor was subjected to ruthenium under a pressure of 3 kg/cm 2 under a nitrogen pressure of 5 μm to obtain a target polyimine precursor. Film formation and hydrazine imidization were carried out in accordance with the method described in Example 1, whereby a pale brown polyester phthalimide film having a film thickness of 25 μm and 12 μηι was obtained, and physical properties were evaluated in the same manner. The physical property values are shown in Table 3. The polyester quinone imine film passes through 180. The bending test also did not break, indicating flexibility. Also, no solubility is exhibited at all for any organic solvent. Further, the polyester phthalimide precursor obtained above was spin-coated on a 6-inch sand wafer by a spin coater (MS-250 'Mikasa Co., Ltd.), and dried at 100 ° C in a drier. After 30 minutes, a non-tacky polystyrene precursor/Shixi wafer laminate (the thickness of the polyuranium precursor layer was 17 μπι) was obtained. Thereafter, in a nitrogen atmosphere, in a hot air dryer, 134489.doc 200948862 at a heating rate of 5 ° C / min, the laminate was subjected to iminomination at i5 ° C for 30 minutes at 200 ° C. The imidization was carried out for 1 hour, and i-imidation was carried out at 400 ° C for 1 hour. Thereafter, the polyester-imide film was peeled off from the twin crystal by hydrofluoric acid to obtain a polyester quinone film having a thickness of 10 μm. A tensile test was conducted on the obtained polyester-imide film to obtain a modulus of elasticity of 54 GPa and a fracture elongation of 53%. Here, the intrinsic viscosity (η) is obtained by measuring 0.5% by mass of a polyesterimide precursor using a Kosher viscosity meter at 301:. ❹

(實施例7) 向300 ml燒瓶中加入10 g之合成例1中獲得之未純化 TABP、150 ml之環丁颯,以油浴加熱至丨⑼它,用3〇分鐘 一面攪拌一面使其溶解。其後,以與實施例丨同樣之方式 進行TABP之評價。用示差掃描熱量計(DSC_6〇,島津製作 所股份有限公司製造)對所獲得之ΤΑΒρ進行測定,結果如 表2所示’熔解熱之峰值溫度⑷為322.5。〇,溫度寬 △T=((bHa))=4.5°C。酸二酐與二胺之投入比為〇.99時分子 量成為最大。又,以〇.99之投入比所獲得之聚酯醯亞胺前 驅物之固有黏度為2·4 dL/g。繼而,依照實施例j、6中所 記栽之方法進行製膜、醯亞胺化,而製作聚酯醯亞胺膜, 同樣地進行物性評價。物性值示於表3。 (比較例1) 向經充分乾燥之附帶攪拌機之密閉反應容器中加入9 27 1之BPIP、再加入48 mi之N_曱基比洛。定酮,將溶液 加溫至8(TC使其溶解。溶解後,向該溶液中緩慢加入9 ^ I34489.doc -52- 200948862 mmol之以式(20)所表示之具有酯結構之四竣酸二酐(以下 稱為TAHQ)。藉由攪拌3 〇分鐘’而使溶液黏度急劇增加。 進而授摔4小時’而獲得透明、均勻且黏稠的聚酯醯亞胺 前驅物溶液: [化 67](Example 7) 10 g of unpurified TABP obtained in Synthesis Example 1 and 150 ml of cyclobutyl hydrazine obtained in Synthesis Example 1 were placed in a 300 ml flask, and heated to an hydrazine (9) in an oil bath, and dissolved while stirring for 3 minutes. . Thereafter, the evaluation of TABP was carried out in the same manner as in Example 。. The obtained ΤΑΒρ was measured by a differential scanning calorimeter (DSC_6〇, manufactured by Shimadzu Corporation), and as a result, the peak temperature (4) of the heat of fusion was 322.5. 〇, the temperature is wide △T=((bHa))=4.5°C. When the ratio of the acid dianhydride to the diamine is 〇.99, the molecular weight becomes the largest. Further, the inherent viscosity of the polyester quinone imine precursor obtained by the input ratio of 〇.99 was 2.4 dL/g. Then, film formation and hydrazine imidization were carried out in accordance with the methods described in Examples j and 6, and a polyesterimine film was produced, and physical properties were evaluated in the same manner. The physical property values are shown in Table 3. (Comparative Example 1) To a well-dried sealed reaction vessel equipped with a stirrer, 9 27 1 of BPIP was added, followed by 48 μ of N_decylbibilol. Ketone, warm the solution to 8 (TC to dissolve it. After dissolution, slowly add 9 ^ I34489.doc -52- 200948862 mmol of tetradecanoic acid with ester structure represented by formula (20) to the solution. A dianhydride (hereinafter referred to as TAHQ). The viscosity of the solution is sharply increased by stirring for 3 ' minutes. Further, it is allowed to fall for 4 hours to obtain a transparent, uniform and viscous polyester phthalimide precursor solution: [Chem. 67]

(20) 〇(20) 〇

❹ 依照實施例1中所記載之方法進行製膜、醯亞胺化,而 製作聚酯醯亞胺臈,同樣地進行物性評價。物性值示於表 1。 該聚酯醯亞胺膜顯示接近於銅箔的線熱膨脹係數、較高 的熱穩定性及可撓性、低彈性率、相對較高的接著性,但 吸濕膨脹係數為7_6 ppm/% RH,相對較高,於26 μηι之聚 酯醯亞胺膜中之撕裂強度為42 mN,較低。又,12 μιη厚 之膜中阻燃性能較低’並未獲得UL94VTM-0之性能。 (比較例2) 於實施例2中,使用TAhQ來代替ΤΑΒΡ,使用1〇49 mol 之APAB、2.62 mol之4,4,-二胺基二苯酯(以ητ稱為〇DA)作 為二胺,除此以外依照實施例2中所記載之方法,使聚酯 醯亞胺前驅物聚合,再進行製膜、醯亞胺化,而製作聚酯 酿亞胺膜,同樣地進行物性評價。物性值示於表1 ^該聚 醋醯亞胺膜顯示接近於銅猪之線熱膨脹係數、較高地熱穩 定性以及可撓性,吸濕膨脹係數為8 3 ppm/。/。RH相對較 134489.doc •53· 200948862 高,彈性率為7·9 GPa較高,接著 強度為0.3 N/mm較低, 於26 μΐΏ之聚醋醯亞胺臈中之 ' 衣·強度為42 mN較低。 又,12 μηι厚之膜中阻燃性能較 _ ^ ., 低並未獲得UL94VTM-0 之性能。 (比較例3) ^ 所表示之二胺(以卜裨马 APB)作為二胺,除此以外依照比較⑴中所記載之方薄膜 Film formation and hydrazine imidization were carried out in accordance with the method described in Example 1 to prepare a polyesterimine oxime, and the physical properties were evaluated in the same manner. The physical property values are shown in Table 1. The polyesterimide film exhibits a linear thermal expansion coefficient close to that of the copper foil, high thermal stability and flexibility, low modulus of elasticity, and relatively high adhesion, but a coefficient of hygroscopic expansion of 7-6 ppm/% RH. , relatively high, the tear strength in the polyester film of 26 μηι is 42 mN, which is lower. Also, the 12 μιη thick film has a low flame retardancy, and the performance of UL94VTM-0 was not obtained. (Comparative Example 2) In Example 2, TAhQ was used instead of hydrazine, and 1 〇 49 mol of APAB and 2.62 mol of 4,4,-diaminodiphenyl ester (referred to as 〇DA by ητ) were used as the diamine. In the same manner as described in Example 2, a polyester phthalimide precursor was polymerized, and then a film was formed and yttrium imidized to prepare a polyester-bromide film, and physical properties were evaluated in the same manner. The physical property values are shown in Table 1. The polyacetal imide film showed a thermal expansion coefficient close to that of the copper pig, high geothermal stability, and flexibility, and the coefficient of hygroscopic expansion was 8 3 ppm/. /. RH is relatively higher than 134489.doc •53·200948862, the elastic modulus is higher at 7·9 GPa, and then the strength is lower than 0.3 N/mm, and the 'clothing strength is 42 in the polyurethane bismuth oxime of 26 μΐΏ. mN is lower. Moreover, the flame retardancy of the film of 12 μηι thick is better than that of _ ^ ., and the performance of UL94VTM-0 is not obtained. (Comparative Example 3) ^ The diamine (in terms of Budma APB) is represented as a diamine, and the other aspects described in the comparison (1) are used.

法’使聚酯醯亞胺前驅物聚合,再進行製臈、醯亞胺化, 而製作聚酯醯亞胺膜,同樣地進行物性評價: [化 68]The method of polymerizing a polyester quinone imine precursor, followed by hydrazine and hydrazine imidization to produce a polyester phthalimide film, and similarly evaluating the physical properties: [Chem. 68]

(2 3) ,物性值不於表1。 該聚酯醯亞胺膜顯示較高的玻璃轉移溫度、較高的接著 性’彈性率顯示較低值為5 2 GPa ’但線熱膨脹係數顯示 較高值為32 ppm/&lt;t,吸濕膨脹係數較高為13 2 ppm/% RH ’於26 μπι之聚酯醯亞胺膜中之撕裂強度為45爪\較 低。又,於焊錫耐熱試驗中發現有鼓起,12 μηι厚之膜中 阻燃性能較低,並未獲得UL94VTM-0之性能。 (比較例4) 於比較例1中,使用實施例1中所獲得之ΤΑΒΡ來代替 TAHQ,使用ΑΡΑΒ作為二胺,除此以外依照比較例1中所 記載之方法’使聚酯醯亞胺前驅物具合,再進行製膜、醯 134489.doc •54· 200948862 亞胺化,而製作聚酯醯亞胺膜,同樣地進行物性評價《物 性值示於表1。該聚酯醯亞胺膜顯示較高的熱穩定性及可 撓性,對低吸濕膨脹係數、高撕裂強度、膜厚12 μιη之聚 醯亞胺膜之阻燃性進行評價後,結果顯示UL94VTM-0之性 能,但線熱膨脹係數為13 ppm/t:,與鋼箔相比顯示較低 的線熱膨脹係數,接著強度為0.4 N/mm較低,彈性率顯示 • 較高值為7.7 GPa。 ❹ 134489.doc •55- 200948862(2 3), the physical property values are not shown in Table 1. The polyesterimide film exhibits a higher glass transition temperature and a higher adhesion. The modulus of elasticity shows a lower value of 5 2 GPa 'but the coefficient of linear thermal expansion shows a higher value of 32 ppm / lt; t, moisture absorption The higher coefficient of expansion is 13 2 ppm/% RH 'the tear strength in the polyester film of 26 μπι is 45 claws\low. Further, in the solder heat resistance test, a bulge was found, and the flame retardancy of the film of 12 μη thick was low, and the performance of UL94VTM-0 was not obtained. (Comparative Example 4) In Comparative Example 1, the ruthenium obtained in Example 1 was used instead of TAHQ, and ruthenium was used as the diamine, and the polyester ruthenium imine precursor was used in accordance with the method described in Comparative Example 1. The material was combined, and then film-forming, 醯134489.doc •54· 200948862 imidization, and a polyester phthalimide film was produced, and the physical property evaluation was performed in the same manner. The physical property values are shown in Table 1. The polyester phthalimide film exhibits high thermal stability and flexibility, and evaluates the flame retardancy of a polyimide film having a low moisture absorption coefficient, a high tear strength, and a film thickness of 12 μm. Shows the performance of UL94VTM-0, but the linear thermal expansion coefficient is 13 ppm/t:, showing a lower coefficient of linear thermal expansion compared to steel foil, followed by a lower strength of 0.4 N/mm, and the modulus of elasticity shows a higher value of 7.7. GPa. ❹ 134489.doc •55- 200948862

撕裂強度 mN (膜厚度) 62 26 μιη 85 26 μιη 80 26 μηι 68 26 μιη 1 72 26 μιη 42 26 μιη i 42 26 μηι 45 26 μιη 73 26 μιη 90度銅箔接著強度 (N/mm) 00 d rn OS 〇 寸 d 彈性率 GPa 寸 ON OO iri ON t&gt; (N in 卜 Γ*^ CHE ppm/%RH wo CN cs cn »〇 m OO 13.2 00 — 阻燃性 VTM-0 〇 〇 〇 〇 〇 X X X 〇 煮沸焊 錫财熱性 〇 〇 〇 〇 〇 〇 〇 X 〇 焊錫 对熱性 〇 〇 〇 〇 〇 〇 〇 X 〇 CTE (Ppm/°C) &lt;N &lt;N CN CS CN Os 卜 cs cn m ^ 6 440 00 5 ry 422 413 ! in $ o cn 453 分子量 133000 103000 115000 107000 74000 143000 114000 104000 84000 組成 (二胺莫耳比) TABP/BPIP TABP/BPIP/APAB (BPIP/APAB=50/50) TABP/BPIP/APAB (BPIP/APAB=70/30) &lt;ζ 〇 &lt; ® 9 JL Oh $ P Oh CQ &amp; H OQ TABP/BPIP/BPTP (BPIP/BPTP=70/30) TAHQ/BPIP TAHQ/APAB/ODA (APAB/ODA=80/20) TAHQ/BAPB ΤΑΒΡ/ΑΡΑΒ 實施例1 實施例2| 實施例3 實施例4 實施例5 比較例1 比較例2 比較例3 比較例4 134489.doc -56- 200948862Tear strength mN (film thickness) 62 26 μηη 85 26 μιη 80 26 μηι 68 26 μιη 1 72 26 μιη 42 26 μιη i 42 26 μηι 45 26 μηη 73 26 μιη 90 degree copper foil strength (N/mm) 00 d Rn OS d d Elasticity rate GPa inch ON OO iri ON t&gt; (N in Γ Γ *^ CHE ppm/%RH wo CN cs cn »〇m OO 13.2 00 — Flame retardant VTM-0 〇〇〇〇〇XXX 〇Boiling soldering heat 〇〇〇〇〇〇〇X 〇Welding to heat 〇〇〇〇〇〇〇X 〇CTE (Ppm/°C) &lt;N &lt;N CN CS CN Os 卜 cn cn m ^ 6 440 00 5 ry 422 413 ! in $ o cn 453 Molecular weight 133000 103000 115000 107000 74000 143000 114000 104000 84000 Composition (diamine molar ratio) TABP/BPIP TABP/BPIP/APAB (BPIP/APAB=50/50) TABP/BPIP/ APAB (BPIP/APAB=70/30) &lt;ζ 〇&lt; ® 9 JL Oh $ P Oh CQ &amp; H OQ TABP/BPIP/BPTP (BPIP/BPTP=70/30) TAHQ/BPIP TAHQ/APAB/ODA (APAB/ODA=80/20) TAHQ/BAPB ΤΑΒΡ/ΑΡΑΒ Example 1 Example 2| Example 3 Example 4 Example 5 Comparative Example 1 Comparative Example 2 Comparative Example 3 Comparative Example 4 13448 9.doc -56- 200948862

溫度寬 T=((b)-(a)) rc) 1___________—_______ &lt;Ν 融解熱峰值溫度 (a) CC) JQ m 322.5 .1 Μ PH 3 CU 3 H H 0 卜 134489.doc 阻燃性 VTM-0 〇 o -=w S ^ 镏拿 m in 彈性率 GPa 寸 uS CHE ppm/% RH 煮沸 焊錫 对熱性 〇 〇 焊錫 耐熱性 〇 〇 90°銅箔 接著強度 kg/cm CTE (ppm/°C) &lt;N CN CM &lt;N ^ 6 〇 〇 寸 寸 清漆 過滤性 o 〇 η (dL/g) 00 CN 寸 CN l.t N U Μ 1« ^ _ Ί绪 0.99 組成 (莫耳比) TABP/BPIP 100/100 TABP/BPIP 100/100 實施例6 實施例7 57· 200948862 [產業上之可利用性] 本發明之聚酯醯亞胺適宜用作各種電子裝置中之電氣絕 緣膜、可撓性印刷配線板、顯示器用基板、電子紙用基 板、太陽電池用基板,尤其適宜用作可撓性印刷配線板用 基材。 【圖式簡單說明】 • 圖1係表示由示差掃描熱量計所顯示之曲線之圖。 ❹Temperature width T=((b)-(a)) rc) 1___________________ &lt;Ν melting peak temperature (a) CC) JQ m 322.5 .1 Μ PH 3 CU 3 HH 0 134489.doc Flame retardant VTM -0 〇o -=w S ^ mm in Elasticity GPa inch uS CHE ppm/% RH Boiled solder for heat 〇〇 solder heat resistance 〇〇90° copper foil strength kg/cm CTE (ppm/°C) &lt;N CN CM &lt;N ^ 6 清 清 varnish filter o (η (dL/g) 00 CN 寸 CN lt NU Μ 1« ^ _ Ί 0.99 0.99 Composition (Mo Erbi) TABP/BPIP 100/100 TABP/BPIP 100/100 Example 6 Example 7 57· 200948862 [Industrial Applicability] The polyester phthalimide of the present invention is suitably used as an electrical insulating film, a flexible printed wiring board, and various electronic devices. The substrate for a display, the substrate for an electronic paper, and the substrate for a solar cell are particularly preferably used as a substrate for a flexible printed wiring board. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a view showing a curve displayed by a differential scanning calorimeter. ❹

134489.doc 58-134489.doc 58-

Claims (1)

200948862 十、申請專利範圍: 1' 一種聚酯醯亞胺前驅物,其特徵在於:具有以卞述 所表示之重複單元: [化1] (1) B γ VH. ❹200948862 X. Patent application scope: 1' A polyester quinone imine precursor characterized by having a repeating unit represented by a description: [1] (1) B γ VH. ❹ (2)(2) (3)(3) (4) (5) 134489.doc (6) 200948862 [化6](4) (5) 134489.doc (6) 200948862 [Chem. 6] [化7][Chemistry 7] [化8][化8] (7) [化9][Chemistry 9] R!表示碳數1〜6之炫基;Rz〜R4表示碳數1〜6之烧基、R! represents a luminescent group having a carbon number of 1 to 6; and Rz to R4 represents a burning group having a carbon number of 1 to 6, 氫原子’該等為分別獨立,可相同亦可不同;R5表示碳 數 2. 如 有 3. 如 有 6之烷基;Re〜R9表示碳數1〜6之烷基、氣原子) 請求項1之聚酯醯亞胺前驅物,其中於式(1)中 以式(3)或式(4)所表示之重複單元。 請求項1之聚酯醯亞胺前驅物,其中於式(1)中 以式(4)所表示之重複單元。 4.如 有 請求項1之聚酯醯亞胺前驅物,其中於式中 以式(10)所表示之重複單元: 134489.doc (10)。 200948862 [化 ίο]The hydrogen atom's are independently independent and may be the same or different; R5 represents a carbon number of 2. If there is 3. an alkyl group of 6; Re~R9 represents an alkyl group having a carbon number of 1 to 6, a gas atom) A polyester quinone imine precursor, wherein the repeating unit represented by the formula (3) or the formula (4) in the formula (1). The polyester quinone imine precursor of claim 1, wherein the repeating unit represented by the formula (4) in the formula (1). 4. The polyester quinone imine precursor of claim 1, wherein the repeating unit represented by formula (10) is: 134489.doc (10). 200948862 [化 ίο] 5. —種聚酯醯亞胺前驅物,其特徵在於:具有以下述式 (11)及式(12)所表示之重複單元,式(11)與式(12)之莫耳 比為式(11)/式(12)=20/80〜80/20之比例: [化 11]A polyester quinone imine precursor having a repeating unit represented by the following formula (11) and formula (12), wherein the molar ratio of the formula (11) and the formula (12) is a formula ( 11) / formula (12) = 20/80 to 80/20 ratio: [Chem. 11] (11) Ar (12)(11) Ar (12) (式(11)及式(12)中,Ar為以式(2)所表示之4價芳香族 基;式(12)中’ Β2為選自式(13)至式(1 7)中之至小—、 2價芳香族基: 種之 [化 12](In the formulae (11) and (12), Ar is a tetravalent aromatic group represented by the formula (2); and in the formula (12), 'Β2 is selected from the formula (13) to the formula (17). To small-, 2-valent aromatic group: species [12] 134489.doc (2) (13) 200948862 [化 13]134489.doc (2) (13) 200948862 [Chem. 13] (14) Ιν(14) Ιν (15) [化 16] (16)(15) [16] (16) [化 17] (17) ;R1G〜R18表示碳數1〜6之烷基、氫原子,該等為分別獨 立,可相同亦可不同)。 6.如請求項5之聚酯醯亞胺前驅物,其中於式(12)中,B2為 以式(16)、式(17)或式(18)所表示之重複單元: 134489.doc (18) 200948862 [化 18](17); R1G to R18 represent an alkyl group having 1 to 6 carbon atoms and a hydrogen atom, and these may be independently and may be the same or different). 6. The polyester quinone imine precursor according to claim 5, wherein in the formula (12), B2 is a repeating unit represented by the formula (16), the formula (17) or the formula (18): 134489.doc ( 18) 200948862 [Chem. 18] 7’如明求項5之聚酯醯亞胺前驅物 以式(16)所表示之重複單元。 8.如4求項丨之聚酯醯亞胺前驅物 為3萬以上、40萬以下。 H求項5之聚醋醯亞胺前驅物 為3萬以上、40萬以下。 10.如印求項6之聚酯醯亞胺前驅物 為3萬以上、40萬以下。 ❹ 其中於式(12)中,B2g ’其重量平均分子量Mw ’其重量平均分子量Mw ’其重量平均分子量Mw η·如咕求項7之聚酯醯亞胺前驅物,其重量平均分子量Mw 為3萬以上、40萬以下。 ❹ 12.如請求項丨之聚酯醯亞胺前驅物,其中獲得該聚酯醯亞 胺前驅物時所使用之以式(19)所表示之含有酯基之四羧 酸二奸,在將由示差掃描熱量計(DSC)所顯示之熔解熱 峰值溫度作為(a) °C、將開始朝向熔解熱波峰上升的溫度 與波峰斜度穩定的温度作為連接點之切線的交點之溫度 設為(b)t,且設定溫度寬AT=((b)-(a)rC時,滿足(a)g 322°C 及 5°C : [化 19]7' The polyester quinone imine precursor of claim 5 is a repeating unit represented by the formula (16). 8. For example, the polyester bismuth imide precursor of the 求 求 为 is 30,000 or more and 400,000 or less. The precursor of the polyacetal imine of claim 5 is 30,000 or more and 400,000 or less. 10. The precursor of the polyester quinone imine of claim 6 is 30,000 or more and 400,000 or less. ❹ In the formula (12), B2g 'its weight average molecular weight Mw 'its weight average molecular weight Mw 'its weight average molecular weight Mw η · such as the polyester ylide precursor of the claim 7, the weight average molecular weight Mw is More than 30,000, less than 400,000. ❹ 12. The polyester quinone imine precursor of the claim ,, wherein the tetracarboxylic carboxylic acid containing the ester group represented by the formula (19) used in obtaining the polyester quinone imine precursor is The peak temperature of the heat of fusion indicated by the differential scanning calorimeter (DSC) is (a) °C, and the temperature at which the temperature at which the peak of the melting heat wave rises and the peak of the peak slope are stabilized as the intersection of the tangent to the joint point is set as (b) )t, and when the temperature is set to AT=((b)-(a)rC, (a)g 322°C and 5°C are satisfied: [Chem. 19] 134489.doc (19)。 200948862 13.如請求項5之聚酯醯亞胺前驅物,其中獲得該聚酯醯亞 胺前驅物時所使用之以式(19)所表示之含有酯基之四羧 酸二酐’在將由示差掃描熱量計(DSC)所顯示之熔解熱 峰值溫度作為(a)°C、將開始朝向熔解熱波峰上升的溫度 與波峰斜度穩定的溫度作為連接點之切線的交點之溫度 設為(b)*t,且設定溫度寬ΔΤ=((1)Η3))β(:時,滿足(a) $ 322 C 及 Δτ 客 5°C : [化 19] ❹ θ134489.doc (19). 200948862 13. The polyester quinone imine precursor according to claim 5, wherein the tetracarboxylic dianhydride containing the ester group represented by the formula (19) used in obtaining the polyester quinone imine precursor is The peak temperature of the heat of fusion indicated by the differential scanning calorimeter (DSC) is (b) °C, and the temperature at which the temperature at which the melting heat peak is raised and the peak of the peak is stabilized as the intersection of the tangent to the joint point is set as (b) )*t, and set the temperature width ΔΤ=((1)Η3))β(:, satisfy (a) $ 322 C and Δτ guest 5°C : [Chem. 19] ❹ θ (19)。 14.如請求項6之聚酯醯亞胺前驅物,其中獲得該聚酯醯亞 胺前驅物時所使用之以式(19)所表示之含有酯基之四缓 酸二酐,在將由示差掃描熱量計(DSC)所顯示之熔解熱 峰值溫度作為(a)。〇、將開始朝向溶解熱波峰上升的溫度 與波峰斜度穩定的溫度作為連接點之切線的交點之溫度 設為(b)°C,且設定溫度寬時’滿足(a) g 322°C 及△TSSt : [化 19](19). 14. The polyester phthalimide precursor of claim 6, wherein the polyester ylide precursor obtained by the formula (19) is an acid-containing tetra-acid dianhydride, which is to be The peak heat of fusion shown by the scanning calorimeter (DSC) is taken as (a). 〇, the temperature at which the temperature rising toward the dissolved heat peak and the temperature at which the peak slope is stable are taken as the intersection of the tangent to the joint point, and the temperature is set to (b) ° C, and when the set temperature is wide, '(a) g 322 ° C and △TSSt : [Chem. 19] (19) 15.如請求項7之聚酯醯亞胺前驅物,其中獲得該聚g旨醯亞 胺則驅物時所使用之以式(19)所表示之含有赌基之四羧 134489.doc 9 200948862 酸二酐,在將由示差掃描熱量計(DSC)所顯示之熔解熱 峰值溫度作為(a)°C、將開始朝向熔解熱波峰上升的溫度 與波峰斜度穩定的溫度作為連接點之切線的交點之溫度 設為(1))°〇,且設定溫度寬么丁=((1))-(&amp;))。(:時,滿足(&amp;)2 322°C 及 ΔΤ$ 5°C : ' [化 19](19) 15. The polyester quinone imine precursor of claim 7, wherein the polyglycolide is obtained by using the ketone-containing tetracarboxyl 134489 represented by the formula (19). Doc 9 200948862 Acid dianhydride, as the junction point, the peak temperature of the heat of fusion indicated by the differential scanning calorimeter (DSC) is (a) °C, and the temperature at which the temperature toward the peak of the melting heat wave is stabilized and the slope of the peak is stabilized. The temperature at the intersection of the tangent is set to (1)) ° 〇, and the set temperature is wide = ((1)) - (&amp;)). (:, (&amp;) 2 322 ° C and ΔΤ $ 5 ° C : ' [Chem. 19] ❹ 16.如請求項11之聚醋醯亞胺前驅物,其中獲得該聚醋醯亞 胺前驅物時所使用之以式(19)所表示之含有酯基之四羧 酸二酐,在將由示差掃描熱量計(DSC)所顯示之熔解熱 峰值溫度作為(a)°C、將開始朝向熔解熱波峰上升的溫度 與波峰斜度穩定的溫度作為連接點之切線的交點之溫度 設為(b)°C,且設定溫度寬ΔΤ=((ΐ3Η&amp;)Γ(:時,滿足(a)g 322°C 及 ΔΤ$ 5°C :❹ 16. The polyacetate precursor of claim 11, wherein the ester-containing tetracarboxylic dianhydride represented by formula (19) used in obtaining the polyacetate precursor is used in The peak temperature of the heat of fusion indicated by the differential scanning calorimeter (DSC) is (b) °C, and the temperature at which the temperature at which the melting heat peak is raised and the peak of the peak is stabilized as the intersection of the tangent to the joint point is set as (b) ) ° C, and set the temperature width Δ Τ = (( ΐ 3 Η &amp;) Γ (:, (a) g 322 ° C and Δ Τ $ 5 ° C: (19) 〇 17. —種聚醋醯亞胺’其特徵在於:其係使如請求 W t聚 酯醯亞胺前驅物醯亞胺化而獲得者。 5之聚 18, 一種聚酯醢亞胺’其特徵在於·•其係使如請求項 酯醯亞胺前驅物醯亞胺化而獲得者。 134489.doc 200948862 19. 一種聚醋醯亞胺,其特徵在於:其係使如請求項6 ^ 酯醯亞胺前驅物醯亞胺化而獲得者。 之聚 20. —種聚酿醯亞胺,其特徵在於:其係使如請求項7之 酯醯亞胺前驅物醯亞胺化而獲得者。 * 21,一種聚酯醯亞胺,其特徵在於:其係使如請求項U之聚 5曰酿亞胺刖驅物酿亞胺化而獲得者。 22. —種聚酯醯亞胺,其特徵在於:其係使如請求項丨5之聚 S曰酿亞胺則驅物酿亞胺化而獲得者。(19) 〇 17. A polyacetamide imino group, which is characterized in that it is obtained by imidating a W t polyester oxime imide precursor. 5 Poly 18, a polyester quinone imine, which is characterized in that it is obtained by imidating the phthalocyanine precursor of the claim. 134489.doc 200948862 19. A polyacetamide imine which is obtained by imidating a phthalocyanine precursor of claim 6 . Poly(polyimide), which is obtained by imidating the ester quinone imine precursor of claim 7. *21, a polyester quinone imine, which is obtained by the imidization of a polyamidene hydrazine hydrazide as claimed in claim U. A polyester quinone imine characterized in that it is obtained by imidating a poly-S-imine of the claim 丨5. 23. —種聚酯醯亞胺,其特徵在於:其係使如請求項16之聚 酯醯亞胺前驅物醯亞胺化而獲得者。 24· —種積層板,其特徵在於:其係具有聚酯醯亞胺層與金 屬層,且該聚酯醯亞胺層係由如請求項17之聚酯醯亞胺 所構成者。 25. —種積層板,其特徵在於:其係具有聚酯醯亞胺層與金 屬層,且該聚酯醯亞胺層係由如請求項18之聚酯醯亞胺 所構成者。 26. —種積層板,其特徵在於··其係具有聚酯醯亞胺層與金 屬層’且該聚醋醯亞胺層係由如請求項19之聚酯醯亞胺 所構成者。 27. —種積層板,其特徵在於:其係具有聚酯醯亞胺層與金 屬層’且該聚酯醯亞胺層係由如請求項2〇之聚酯醯亞胺 所構成者。 28. —種積層板,其特徵在於:其係具有聚酯醯亞胺層與金 屬層’且該聚酯醯亞胺層係由如請求項21之聚酯醯亞胺 134489.doc 200948862 所構成者。 29. —種積層板,其特徵在於:其係具有聚酯醯亞胺層與金 屬層’且該聚酯醢亞胺層係由如請求項22之聚酯醯亞胺 所構成者。 30. —種積層板,其特徵在於:其係具有聚酯醯亞胺層與金 屬層,且該聚酯醯亞胺層係由如請求項23之聚酯醯亞胺 所構成者。 ❹A polyester quinone imine which is obtained by imidating a polyester oxime imide precursor of claim 16. A laminate comprising a polyester quinone layer and a metal layer, and the polyester quinone layer is composed of the polyester quinone imine of claim 17. A laminated board characterized by comprising a polyester quinone layer and a metal layer, and the polyester quinone layer is composed of the polyester quinone imine of claim 18. A laminated board characterized in that it has a polyester quinone layer and a metal layer ' and the acetazide layer is composed of the polyester quinone imine of claim 19. 27. A laminate comprising: a polyester quinone layer and a metal layer&apos; and the polyester quinone layer is comprised of the polyester quinone imine of claim 2. 28. A laminate comprising: a polyester quinone layer and a metal layer ' and the polyester quinone layer is comprised of the polyester quinone imine 134489.doc 200948862 of claim 21. By. 29. A laminate comprising: a polyester quinone layer and a metal layer&apos; and the polyester quinone layer is comprised of the polyester quinone imine of claim 22. 30. A laminated board characterized by having a polyester quinone layer and a metal layer, and the polyester quinone layer is composed of the polyester quinone imine of claim 23. ❹ 31.如請求項24之積層板,其係藉由將如請求項1之聚醋醯 亞胺前驅物塗布於金屬箔上,乾燥後,進行加熱或者利 用脫水試劑使其醯亞胺化而獲得者。 32.如請求項25之積層板,其係藉由將如請求項$之聚酯醯 亞胺前驅物塗布於金屬箱上,乾燥後,進行加熱或者利 用脫水試劑使其醯亞胺化而獲得者。 33.如請求項26之積層板,其係藉由將如請求項6之聚醋醯 亞胺前驅物塗布於金屬落上,乾燥後,進行加熱或者利 用脫水試劑使其醯亞胺化而獲得者。 34·如請求項27之積層板,其係藉由將如請求^之聚㈣ 亞胺前驅物塗布於金屬箱上,乾燥後,進行加熱或者利 用脫水试劑使其酿亞胺化而獲得者。 3 5.如請求項28之積層板,其係藉由蔣如抹 τ褙田將如蜎求項11之聚酯醯 亞胺前驅物塗布於金屬羯上,乾燥後,進行加熱或者利 用脫水試劑使其醯亞胺化而獲得者。 36.如請求項29之積層板,其係藉由將如請求項以㈣酿 亞胺前驅物塗布於金屬_上’乾燥後,進行加熱或者利 134489.doc 200948862 用脫水試劑使其醯亞胺化而獲得者。 37.如請求項3〇之積層板,其係藉由將如請求項16之聚醋醯 亞胺前驅物塗布於金屬笛上,乾燥後,進行加熱 用脫水試劑使其酿亞胺化而獲得者。 ❹31. The laminate of claim 24, which is obtained by applying the polyacetal imide precursor of claim 1 to a metal foil, drying it, heating it, or imidating the hydrazine with a dehydrating reagent. By. 32. The laminate of claim 25, which is obtained by applying a polyester phthalimide precursor as claimed in claim A to a metal box, drying, heating or denitrifying the hydrazine with a dehydrating reagent. By. 33. The laminate of claim 26, which is obtained by applying a polyacetal imide precursor as claimed in claim 6 to a metal drop, drying it, heating it, or imidating the hydrazine with a dehydrating reagent. By. 34. The laminate according to claim 27, which is obtained by applying a poly(tetra)imine precursor as claimed to a metal case, drying it, heating it, or aminating it with a dehydrating reagent. . 3 5. The laminate of claim 28, which is coated with a polyester bismuth imide precursor of claim 11 on a metal crucible by Jiang Rumo, and dried, heated or dehydrated. The one obtained by imidating the oxime. 36. The laminate of claim 29, which is heated by a coating of the (IV)-imine precursor prior to drying on the metal as described in the request, or by 134489.doc 200948862 using a dehydrating reagent to make the quinone imine The winner. 37. The laminate according to claim 3, which is obtained by coating a polyacetate precursor of claim 16 on a metal flute, drying it, and heating it with a dehydrating reagent to imidize it. By. ❹ 134489.doc134489.doc
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