TWI775946B - Polyimide powder, polyimide coating and polyimide film - Google Patents

Polyimide powder, polyimide coating and polyimide film Download PDF

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TWI775946B
TWI775946B TW107132906A TW107132906A TWI775946B TW I775946 B TWI775946 B TW I775946B TW 107132906 A TW107132906 A TW 107132906A TW 107132906 A TW107132906 A TW 107132906A TW I775946 B TWI775946 B TW I775946B
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polyimide
polyimide powder
powder
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TW201915050A (en
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田中圭三
山田俊輔
長島豊
清水誠吾
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日商河村產業股份有限公司
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    • 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
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    • 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
    • C08G73/1039Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors comprising halogen-containing substituents
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    • 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
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    • C08G73/1075Partially aromatic polyimides
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    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G73/00Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
    • C08G73/06Polycondensates having nitrogen-containing heterocyclic rings in the main chain of the macromolecule
    • C08G73/10Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
    • C08G73/1075Partially aromatic polyimides
    • C08G73/1078Partially aromatic polyimides wholly aromatic in the diamino moiety
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
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    • 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
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    • C09D179/00Coating compositions based on 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 C09D161/00 - C09D177/00
    • C09D179/04Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
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    • C08J2379/00Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen, or carbon only, not provided for in groups C08J2361/00 - C08J2377/00
    • C08J2379/04Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
    • C08J2379/08Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
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Abstract

本發明為一種聚醯亞胺粉體,其係由聚醯亞胺粉體A與聚醯亞胺粉體B的混合所構成,且為可溶於有機溶媒的聚醯亞胺粉體,其特徵為聚醯亞胺粉體A及聚醯亞胺粉體B,分別由具有源自至少1種類的芳香族二胺化合物之構造單位與源自至少1種類四羧酸二酐之構造單位的聚醯亞胺所構成,聚醯亞胺粉體A係由具有(a-1)1.2dL/g以上且未滿2.1dL/g之還原黏度,或(a-2)100,000g/mol以上且未滿250,000g/mol之重量平均分子量的聚醯亞胺所構成,聚醯亞胺粉體B係由具有(b-1)2.1dL/g以上3.0dL/g以下之還原黏度,或(b-2)250,000g/mol以上500,000g/mol以下之重量平均分子量的聚醯亞胺所構成,聚醯亞胺粉體A/聚醯亞胺粉體B的重量比為10/90~90/10的範圍,對於聚醯亞胺粉體A與聚醯亞胺粉體B的混合所測定之還原黏度為1.7~2.5dL/g的範圍,或對於聚醯亞胺粉體A與聚醯亞胺粉體B的混合所測定之重量平均分子量為160,000~350,000g/mol的範圍,該聚醯亞胺粉體可溶於有機溶媒且操作性優異,將該聚醯亞胺粉體以指定的濃度溶解在有機溶媒之塗料,賦予耐熱性、透明性及機械特性優異之聚醯亞胺薄膜。The present invention is a polyimide powder, which is composed of a mixture of polyimide powder A and polyimide powder B, and is a polyimide powder soluble in organic solvents. It is characterized in that the polyimide powder A and the polyimide powder B are respectively composed of a structural unit derived from at least one kind of aromatic diamine compound and a structural unit derived from at least one kind of tetracarboxylic dianhydride. It is composed of polyimide, and the polyimide powder A is composed of (a-1) a reduced viscosity of 1.2 dL/g or more and less than 2.1 dL/g, or (a-2) 100,000 g/mol or more and It is composed of polyimide with a weight-average molecular weight of less than 250,000 g/mol, and the polyimide powder B has a reduced viscosity of (b-1) 2.1 dL/g or more and 3.0 dL/g or less, or (b -2) It is composed of polyimide with a weight average molecular weight of 250,000 g/mol or more and 500,000 g/mol or less, and the weight ratio of polyimide powder A/polyimide powder B is 10/90~90/ In the range of 10, the reduced viscosity measured for the mixture of polyimide powder A and polyimide powder B is in the range of 1.7 to 2.5 dL/g, or for polyimide powder A and polyimide powder B The weight average molecular weight measured by mixing the amine powder B is in the range of 160,000 to 350,000 g/mol. The polyimide powder is soluble in organic solvents and has excellent handleability. Coatings dissolved in an organic solvent at a concentration give a polyimide film with excellent heat resistance, transparency and mechanical properties.

Description

聚醯亞胺粉體、聚醯亞胺塗料及聚醯亞胺薄膜Polyimide powder, polyimide coating and polyimide film

本發明係關於聚醯亞胺粉體及使用其所得之聚醯亞胺塗料以及聚醯亞胺薄膜,尤其是關於適合使用在顯示器用途或電子材料用途,給予兼具極為優異之耐熱性與透明性的聚醯亞胺薄膜的聚醯亞胺粉體及聚醯亞胺塗料。The present invention relates to polyimide powders and polyimide coatings and polyimide films obtained by using the same, especially for use in display applications or electronic material applications, providing both extremely excellent heat resistance and transparency. Polyimide powder and polyimide coating of polyimide film.

聚醯亞胺樹脂作為耐熱性優異之高分子,被活用於航空宇宙領域、電氣絕緣領域、電子領域等之要求耐熱性或高信賴性的廣泛領域。又,近年來已提案有兼備耐熱性與透明性之透明聚醯亞胺,例如專利文獻1中提案有由含有氟原子之特定單體所合成之適合於光導波之透明性優異的可溶性聚醯亞胺。專利文獻2中提案有可溶於使用特定之脂環式二胺的有機溶劑的透明聚醯亞胺。然而,專利文獻1及專利文獻2中關於聚醯亞胺粉體並未揭示,且由於專利文獻2所記載之聚醯亞胺係將脂環式之二胺作為原料使用,缺乏耐熱性,有因加熱導致著色的問題。Polyimide resins, as polymers with excellent heat resistance, are used in a wide range of fields requiring heat resistance or high reliability, such as aerospace, electrical insulation, and electronics. In addition, in recent years, transparent polyimide having both heat resistance and transparency has been proposed. For example, Patent Document 1 proposes a soluble polyimide, which is synthesized from a specific monomer containing a fluorine atom and is suitable for optical waveguides and has excellent transparency. imine. Patent Document 2 proposes a transparent polyimide that is soluble in an organic solvent using a specific alicyclic diamine. However, Patent Document 1 and Patent Document 2 do not disclose the polyimide powder, and since the polyimide described in Patent Document 2 uses an alicyclic diamine as a raw material, it lacks heat resistance and has Problems with coloring due to heating.

作為聚醯亞胺之粉體,揭示有於可溶性聚醯亞胺之塗料添加水或甲醇等之貧溶媒,使塊狀之聚醯亞胺樹脂析出之方法(專利文獻3)。As a powder of polyimide, a method of depositing a block-shaped polyimide resin by adding a poor solvent such as water or methanol to a coating material of soluble polyimide is disclosed (Patent Document 3).

又,專利文獻4中提案有聚合二胺類與酸二酐類所得之聚醯胺酸的醯亞胺化物之粉末。Moreover, in patent document 4, the powder of the imide compound of polyamic acid obtained by polymerizing diamines and acid dianhydrides is proposed.

然而,專利文獻3或專利文獻4所記載之聚醯亞胺的粉體,雖係將原料單體之二胺類的莫耳量與酸酐的莫耳量基本上定為相同,經由經聚合之聚醯胺酸來製造,但如此之製造方法的情況,因僅單體之秤量誤差、單體之溶解殘留、單體之純度的變動等,而導致聚醯胺酸之聚合度大幅變動,作為結果,有所得之聚醯亞胺粉體的聚合度無法安定的問題。為了防止此點,雖截取將二胺與酸酐之莫耳量的比率從1移動些微,進行聚醯胺酸聚合之方法,但即使該情況下,亦有因溶媒中所包含之水分量的影響導致聚合度變動的問題。又,於聚醯胺酸溶液之階段,即使為同等之聚合度的溶液,即使在之後的醯亞胺化、粉體化、乾燥等之步驟,亦有產生因聚合物之分裂等導致聚合度變化的問題的情況。However, the powder of the polyimide described in Patent Document 3 or Patent Document 4 is based on the fact that the molar amount of the diamines and the molar amount of the acid anhydride are basically the same as the raw material monomers. However, in the case of such a production method, the degree of polymerization of the polyamic acid greatly varies due to only the weighing error of the monomer, the dissolved residue of the monomer, and the fluctuation of the purity of the monomer. As a result, there is a problem that the degree of polymerization of the obtained polyimide powder cannot be stabilized. In order to prevent this, a method of polymerizing polyamic acid by slightly shifting the molar ratio of diamine and acid anhydride from 1 is adopted. However, even in this case, it is affected by the amount of water contained in the solvent. Problems that cause changes in the degree of aggregation. In addition, in the stage of the polyamic acid solution, even if it is a solution with the same degree of polymerization, even in the subsequent steps of imidization, powderization, drying, etc., the degree of polymerization may be caused by the splitting of the polymer. Change the situation of the problem.

如此,將聚合度變動之聚醯亞胺粉體直接溶解在溶媒,作為聚醯亞胺溶液(塗料)使用時,有聚醯亞胺塗料的黏度顯著變動,無法成為安定之聚醯亞胺薄膜的製膜,並且有降低所得之聚醯亞胺薄膜的機械特性的例子的問題。 [先前技術文獻] [專利文獻]In this way, when the polyimide powder with varying degrees of polymerization is directly dissolved in a solvent and used as a polyimide solution (coating), the viscosity of the polyimide coating changes significantly, and a stable polyimide film cannot be obtained. film formation, and there is a problem of lowering the mechanical properties of the resulting polyimide film. [Prior Art Literature] [Patent Literature]

[專利文獻1] 日本特開平4-235505   [專利文獻2] 日本特開2000-169579   [專利文獻3] 日本特開2004-285355   [專利文獻4] 日本特表2013-523939[Patent Document 1] Japanese Patent Laid-Open No. 4-235505 [Patent Document 2] Japanese Patent Laid-Open No. 2000-169579 [Patent Document 3] Japanese Patent Laid-Open No. 2004-285355 [Patent Document 4] Japanese Patent Publication 2013-523939

[發明欲解決之課題][The problem to be solved by the invention]

本發明之目的係給予耐熱性、透明性及機械特性優異之聚醯亞胺薄膜,給予可溶於有機溶媒且操作性優異之聚醯亞胺粉體及聚醯亞胺塗料。 [用以解決課題之手段]The object of the present invention is to provide a polyimide film excellent in heat resistance, transparency and mechanical properties, a polyimide powder and a polyimide coating that are soluble in organic solvents and excellent in handleability. [means to solve the problem]

本發明者們發現藉由將具有不同還原黏度或重量平均分子量的聚醯亞胺粉體A與聚醯亞胺粉體B,以特定的範圍的重量比率進行混合,而得到給予耐熱性、透明性及機械特性極為優異之聚醯亞胺薄膜的操作性良好之聚醯亞胺粉體及聚醯亞胺塗料,而完成本發明。The present inventors found that by mixing polyimide powder A and polyimide powder B having different reduction viscosities or weight average molecular weights in a specific range of weight ratios, it is possible to obtain heat-resistant, transparent The present invention has been completed by a polyimide film having excellent properties and mechanical properties, a polyimide powder having good handleability, and a polyimide coating.

根據本發明,提供一種以下所示之聚醯亞胺粉體、聚醯亞胺塗料、聚醯亞胺塗料的製造方法及聚醯亞胺薄膜。   [1] 一種聚醯亞胺粉體,其係由聚醯亞胺粉體A與聚醯亞胺粉體B的混合所構成,且為可溶於有機溶媒的聚醯亞胺粉體,其特徵為聚醯亞胺粉體A及聚醯亞胺粉體B,分別由具有源自至少1種類的芳香族二胺化合物之構造單位與源自至少1種類四羧酸二酐之構造單位的聚醯亞胺所構成,   聚醯亞胺粉體A係由具有(a-1)1.2dL/g以上且未滿2.1dL/g之還原黏度,或(a-2)100,000g/mol以上且未滿250,000g/mol之重量平均分子量的聚醯亞胺所構成,   聚醯亞胺粉體B係由具有(b-1)2.1dL/g以上3.0dL/g以下之還原黏度,或(b-2)250,000g/mol以上500,000g/mol以下之重量平均分子量的聚醯亞胺所構成,   聚醯亞胺粉體A/聚醯亞胺粉體B的重量比為10/90~90/10的範圍,   對於聚醯亞胺粉體A與聚醯亞胺粉體B的混合所測定之還原黏度為1.7~2.5dL/g的範圍,或對於聚醯亞胺粉體A與聚醯亞胺粉體B的混合所測定之重量平均分子量為160,000~350,000g/mol的範圍。   [2] 如[1]所記載之聚醯亞胺粉體,其中,聚醯亞胺粉體A係由具有(a-1)1.2dL/g以上且未滿2.1dL/g之還原黏度的聚醯亞胺所構成,聚醯亞胺粉體B係由具有(b-1)2.1dL/g以上3.0dL/g以下之還原黏度的聚醯亞胺所構成,對於聚醯亞胺粉體A與聚醯亞胺粉體B的混合所測定之還原黏度為1.7~2.5dL/g的範圍。   [3] 如[1]所記載之聚醯亞胺粉體,其中,聚醯亞胺粉體A係由具有(a-2)100,000g/mol以上且未滿250,000g/mol之重量平均分子量的聚醯亞胺所構成,聚醯亞胺粉體B係由具有(b-2)250,000g/mol以上500,000g/mol以下之重量平均分子量的聚醯亞胺所構成,對於聚醯亞胺粉體A與聚醯亞胺粉體B的混合所測定之重量平均分子量為160,000~350,000g/mol的範圍。   [4] 如[1]~[3]中任一項之聚醯亞胺粉體,其係於前述至少1種類的芳香族二胺化合物,包含至少1種類具有氟基之芳香族二胺化合物。   [5] 如[1]~[4]中任一項之聚醯亞胺粉體,其係於前述至少1種類的四羧酸二酐,包含至少1種類具有氟基之芳香族四羧酸二酐。   [6] 如[1]~[5]中任一項之聚醯亞胺粉體,其中,聚醯亞胺粉體A與聚醯亞胺粉體B係由具有源自同一芳香族二胺化合物之構造單位與源自同一四羧酸二酐之構造單位的聚醯亞胺所構成。   [7] 如[1]~[6]中任一項之聚醯亞胺粉體,其中,聚醯亞胺粉體A及聚醯亞胺粉體B皆為由經由對聚醯胺酸之聚合、化學醯亞胺化反應、藉由生成聚醯亞胺的析出之粉體的形成及乾燥之步驟所製造之聚醯亞胺所構成。   [8] 如[1]~[7]中任一項之聚醯亞胺粉體,其中,前述對於聚醯亞胺粉體A與聚醯亞胺粉體B的混合所測定之平均粒徑為0.02~0.8mm的範圍。   [9] 如[1]~[8]中任一項之聚醯亞胺粉體,其中,從溶解在有機溶媒之溶液進行製膜所得之厚度50μm的聚醯亞胺薄膜,給予85%以上之全光線透過率及-3~3的範圍之黃色度(Yellow Index)。   [10] 一種聚醯亞胺塗料,其特徵為於有機溶媒中,如[1]~[9]中任一項之聚醯亞胺粉體以1~30重量%的濃度溶解。   [11] 一種如[10]所記載之聚醯亞胺塗料的製造方法,其係包含將聚醯亞胺粉體A以成為1~30重量%的濃度的方式溶解在有機溶媒的塗料、與將聚醯亞胺粉體B以成為1~30重量%的濃度的方式溶解在有機溶媒的塗料,以聚醯亞胺粉體A/聚醯亞胺粉體B的重量比成為10/90~90/10的範圍的方式進行混合,其中,該聚醯亞胺粉體A係由具有源自至少1種類的芳香族二胺化合物之構造單位與源自至少1種類四羧酸二酐之構造單位,且具有可溶於有機溶媒的(a-1)1.2dL/g以上且未滿2.1dL/g之還原黏度,或(a-2)100,000g/mol以上且未滿250,000g/mol之重量平均分子量的聚醯亞胺所構成,該聚醯亞胺粉體B係由具有源自至少1種類的芳香族二胺化合物之構造單位與源自至少1種類四羧酸二酐之構造單位,且具有可溶於有機溶媒的(b-1)2.1dL/g以上3.0dL/g以下之還原黏度,或(b-2)100,000g/mol以上且未滿250,000g/mol之重量平均分子量的聚醯亞胺所構成。   [12] 如[11]所記載之聚醯亞胺塗料的製造方法,其中,前述塗料為將聚醯亞胺粉體A以成為1~30重量%的濃度的方式溶解在有機溶媒的塗料、與將聚醯亞胺粉體B以成為1~30重量%的濃度的方式溶解在有機溶媒的塗料,該聚醯亞胺粉體A係由具有源自至少1種類的芳香族二胺化合物之構造單位與源自至少1種類四羧酸二酐之構造單位,且具有可溶於有機溶媒的(a-1)1.2dL/g以上且未滿2.1dL/g之還原黏度的聚醯亞胺所構成,該聚醯亞胺粉體B係由具有源自至少1種類的芳香族二胺化合物之構造單位與源自至少1種類四羧酸二酐之構造單位,且具有可溶於有機溶媒的(b-1)2.1dL/g以上3.0dL/g以下之還原黏度的聚醯亞胺所構成。   [13] 如[11]所記載之聚醯亞胺塗料的製造方法,其中,前述塗料為將聚醯亞胺粉體A以成為1~30重量%的濃度的方式溶解在有機溶媒的塗料、與將聚醯亞胺粉體B以成為1~30重量%的濃度的方式溶解在有機溶媒的塗料,該聚醯亞胺粉體A係由具有源自至少1種類的芳香族二胺化合物之構造單位與源自至少1種類四羧酸二酐之構造單位,且具有可溶於有機溶媒的(a-2)100,000g/mol以上且未滿250,000g/mol之重量平均分子量的聚醯亞胺所構成,該聚醯亞胺粉體B係具有源自至少1種類的芳香族二胺化合物之構造單位與源自至少1種類四羧酸二酐之構造單位,且具有可溶於有機溶媒的(b-2)100,000g/mol以上且未滿250,000g/mol之重量平均分子量的聚醯亞胺所構成。   [14] 一種聚醯亞胺薄膜,其係製膜如[10]所記載之聚醯亞胺塗料所得。   [15] 如[14]所記載之聚醯亞胺薄膜,其中,全光線透過率為85%以上,且黃色度為-3~3的範圍。 [發明的效果]According to the present invention, a polyimide powder, a polyimide coating material, a method for producing a polyimide coating material, and a polyimide film shown below are provided. [1] A polyimide powder, which is composed of a mixture of polyimide powder A and polyimide powder B, and is a polyimide powder soluble in an organic solvent, which is It is characterized in that the polyimide powder A and the polyimide powder B are respectively composed of a structural unit derived from at least one kind of aromatic diamine compound and a structural unit derived from at least one kind of tetracarboxylic dianhydride. The polyimide powder A is composed of (a-1) a reduced viscosity of 1.2 dL/g or more and less than 2.1 dL/g, or (a-2) 100,000 g/mol or more and It is composed of polyimide with a weight-average molecular weight of less than 250,000 g/mol. -2) It is composed of polyimide with a weight average molecular weight of 250,000 g/mol or more and 500,000 g/mol or less, and the weight ratio of polyimide powder A/polyimide powder B is 10/90~90/ In the range of 10, the reduced viscosity measured for the mixture of polyimide powder A and polyimide powder B is in the range of 1.7 to 2.5 dL/g, or for polyimide powder A and polyimide powder B The weight average molecular weight measured by mixing the amine powder B is in the range of 160,000 to 350,000 g/mol. [2] The polyimide powder according to [1], wherein the polyimide powder A is made of a polyimide powder having (a-1) a reduced viscosity of 1.2 dL/g or more and less than 2.1 dL/g It is composed of polyimide, and the polyimide powder B is composed of (b-1) a polyimide having a reducing viscosity of not less than 2.1 dL/g and not more than 3.0 dL/g. The reduced viscosity measured by mixing A and the polyimide powder B was in the range of 1.7 to 2.5 dL/g. [3] The polyimide powder according to [1], wherein the polyimide powder A has (a-2) a weight average molecular weight of 100,000 g/mol or more and less than 250,000 g/mol The polyimide powder B is composed of (b-2) a polyimide having a weight average molecular weight of not less than 250,000 g/mol and not more than 500,000 g/mol. The weight average molecular weight measured by mixing the powder A and the polyimide powder B is in the range of 160,000 to 350,000 g/mol. [4] The polyimide powder according to any one of [1] to [3], which is based on the at least one kind of aromatic diamine compound and includes at least one kind of aromatic diamine compound having a fluorine group . [5] The polyimide powder according to any one of [1] to [4], which is based on the aforementioned at least one type of tetracarboxylic dianhydride and contains at least one type of aromatic tetracarboxylic acid having a fluorine group Dianhydride. [6] The polyimide powder according to any one of [1] to [5], wherein the polyimide powder A and the polyimide powder B are composed of a polyimide derived from the same aromatic diamine The structural unit of the compound is composed of a polyimide derived from the structural unit of the same tetracarboxylic dianhydride. [7] The polyimide powder according to any one of [1] to [6], wherein both the polyimide powder A and the polyimide powder B are made of p-polyimide Polymerization, chemical imidization reaction, and polyimide produced by the steps of forming and drying the precipitated powder of polyimide. [8] The polyimide powder according to any one of [1] to [7], wherein the average particle diameter measured for the mixture of the polyimide powder A and the polyimide powder B It is the range of 0.02-0.8mm. [9] The polyimide powder according to any one of [1] to [8], wherein a polyimide film having a thickness of 50 μm obtained by film formation from a solution dissolved in an organic solvent has a concentration of 85% or more The total light transmittance and the yellowness in the range of -3 to 3 (Yellow Index). [10] A polyimide coating, characterized in that the polyimide powder of any one of [1] to [9] is dissolved in an organic solvent at a concentration of 1 to 30% by weight. [11] A method for producing a polyimide paint according to [10], which comprises a paint in which polyimide powder A is dissolved in an organic solvent at a concentration of 1 to 30% by weight, and A paint in which polyimide powder B is dissolved in an organic solvent at a concentration of 1 to 30% by weight, and the weight ratio of polyimide powder A/polyimide powder B is 10/90 to The polyimide powder A is mixed in a 90/10 range, wherein the polyimide powder A is composed of a structural unit derived from at least one kind of aromatic diamine compound and a structure derived from at least one kind of tetracarboxylic dianhydride. unit, and has a reduced viscosity of (a-1) 1.2 dL/g or more and less than 2.1 dL/g, or (a-2) 100,000 g/mol or more and less than 250,000 g/mol It is composed of polyimide having a weight average molecular weight, and the polyimide powder B is composed of a structural unit derived from at least one type of aromatic diamine compound and a structural unit derived from at least one type of tetracarboxylic dianhydride. , and has a reduced viscosity of (b-1) 2.1 dL/g or more and 3.0 dL/g or less, or (b-2) a weight average molecular weight of 100,000 g/mol or more and less than 250,000 g/mol that is soluble in organic solvents of polyimide. [12] The method for producing a polyimide coating material according to [11], wherein the coating material is a coating material obtained by dissolving the polyimide powder A in an organic solvent at a concentration of 1 to 30% by weight, In contrast to the coating material in which the polyimide powder B is dissolved in an organic solvent at a concentration of 1 to 30% by weight, the polyimide powder A is composed of a compound having an aromatic diamine compound derived from at least one species. A structural unit and a structural unit derived from at least one type of tetracarboxylic dianhydride, and having (a-1) a polyimide having a reduced viscosity of 1.2 dL/g or more and less than 2.1 dL/g soluble in an organic solvent Formed, the polyimide powder B is composed of a structural unit derived from at least one kind of aromatic diamine compound and a structural unit derived from at least one kind of tetracarboxylic dianhydride, and has a soluble organic solvent. (b-1) It is composed of polyimide with a reduced viscosity of not less than 2.1dL/g and not more than 3.0dL/g. [13] The method for producing a polyimide coating material according to [11], wherein the coating material is a coating material obtained by dissolving the polyimide powder A in an organic solvent at a concentration of 1 to 30% by weight, In contrast to the coating material in which the polyimide powder B is dissolved in an organic solvent at a concentration of 1 to 30% by weight, the polyimide powder A is composed of a compound having an aromatic diamine compound derived from at least one species. A structural unit and a structural unit derived from at least one type of tetracarboxylic dianhydride, and having a weight-average molecular weight of (a-2) soluble in an organic solvent of 100,000 g/mol or more and less than 250,000 g/mol Consisting of amines, the polyimide powder B has a structural unit derived from at least one type of aromatic diamine compound and a structural unit derived from at least one type of tetracarboxylic dianhydride, and is soluble in an organic solvent (b-2) is composed of polyimide having a weight average molecular weight of 100,000 g/mol or more and less than 250,000 g/mol. [14] A polyimide film, which is obtained from the polyimide coating described in [10]. [15] The polyimide film according to [14], wherein the total light transmittance is 85% or more, and the yellowness is in the range of -3 to 3. [Effect of invention]

藉由本發明,可提供一種給予具有優異之耐熱性或機械特性,且透明性亦優異之聚醯亞胺薄膜的聚醯亞胺粉體及聚醯亞胺塗料。According to the present invention, it is possible to provide a polyimide powder and a polyimide coating material that provide a polyimide film having excellent heat resistance or mechanical properties and also excellent in transparency.

本發明之第一實施態樣之聚醯亞胺粉體,係藉由將聚醯亞胺粉體A與聚醯亞胺粉體B以重量比率,即以聚醯亞胺粉體A/聚醯亞胺粉體B=10/90~90/10的比率進行混合,以對於所得之混合所測定之還原黏度調整為1.7~2.5dL/g的範圍,或以對於所得之混合所測定之重量平均分子量調整為160,000~350,000g/mol的範圍來製造,而該聚醯亞胺粉體A係由使用芳香族二胺化合物與四羧酸二酐所製造之(a-1)還原黏度為1.2dL/g以上且未滿2.1dL/g之聚醯亞胺,或(a-2)重量平均分子量為100,000g/mol以上且未滿250,000g/mol之聚醯亞胺所構成,該聚醯亞胺粉體B係由(b-1)還原黏度為2.1dL/g以上3.0dL/g以下之聚醯亞胺,或(b-2)重量平均分子量為250,000g/mol以上500,000g/mol以下之聚醯亞胺所構成。The polyimide powder of the first embodiment of the present invention is prepared by mixing the polyimide powder A and the polyimide powder B in a weight ratio, that is, the polyimide powder A/polyimide powder The imide powder B is mixed at a ratio of 10/90 to 90/10, and the reduced viscosity measured for the resulting mixture is adjusted to be in the range of 1.7 to 2.5 dL/g, or the weight measured for the resulting mixture The average molecular weight is adjusted in the range of 160,000 to 350,000 g/mol, and the polyimide powder A is produced by using an aromatic diamine compound and a tetracarboxylic dianhydride (a-1) The reduced viscosity is 1.2 dL/g or more and less than 2.1dL/g of polyimide, or (a-2) polyimide with a weight-average molecular weight of 100,000 g/mol or more and less than 250,000 g/mol, the polyimide The imine powder B is composed of (b-1) polyimide with reduced viscosity of 2.1dL/g or more and 3.0dL/g or less, or (b-2) weight average molecular weight of 250,000g/mol or more and 500,000g/mol It consists of the following polyimide.

本發明之第二實施態樣之聚醯亞胺塗料,係藉由將聚醯亞胺粉體A與聚醯亞胺粉體B以重量比,即以聚醯亞胺粉體A/聚醯亞胺粉體B=10/90~90/10的比率進行混合,將以對於所得之混合所測定之還原黏度調整為1.7~2.5dL/g的範圍,或以對於所得之混合所測定之重量平均分子量調整為160,000~350,000g/mol的範圍的聚醯亞胺粉體,以成為1~30重量%的濃度的方式溶解在有機溶媒,來製造,而該聚醯亞胺粉體A係由使用芳香族二胺化合物與四羧酸二酐所製造之(a-1)還原黏度為1.2dL/g以上且未滿2.1dL/g,或(a-2)重量平均分子量為100,000g/mol以上且未滿250,000g/mol之聚醯亞胺所構成,該聚醯亞胺粉體B係由(b-1)還原黏度為2.1dL/g以上3.0dL/g以下之聚醯亞胺,或(b-2)重量平均分子量為250,000g/mol以上500,000g/mol以下之聚醯亞胺所構成。又,聚醯亞胺塗料亦可藉由將前述聚醯亞胺粉體A與聚醯亞胺粉體B分別以濃度成為1~30%的濃度的方式,溶解在有機溶媒後,以溶質之聚醯亞胺A與聚醯亞胺B的重量比率成為聚醯亞胺A/聚醯亞胺B=10/90~90/10的方式進行混合,來製造。The polyimide coating of the second embodiment of the present invention is prepared by mixing polyimide powder A and polyimide powder B in a weight ratio, that is, polyimide powder A/polyimide powder The imine powder B is mixed at a ratio of 10/90 to 90/10, and the reduced viscosity measured for the resulting mixture is adjusted to a range of 1.7 to 2.5 dL/g, or the weight measured for the resulting mixture is adjusted A polyimide powder having an average molecular weight adjusted to a range of 160,000 to 350,000 g/mol is produced by dissolving it in an organic solvent at a concentration of 1 to 30% by weight, and the polyimide powder A is made of (a-1) Reduced viscosity of 1.2 dL/g or more and less than 2.1 dL/g, or (a-2) Weight average molecular weight of 100,000 g/mol, produced using an aromatic diamine compound and tetracarboxylic dianhydride The polyimide powder B is composed of a polyimide of more than 250,000 g/mol and less than 250,000 g/mol. Or (b-2) It consists of polyimide whose weight average molecular weight is 250,000 g/mol or more and 500,000 g/mol or less. In addition, the polyimide coating can also be dissolved in an organic solvent by dissolving the aforementioned polyimide powder A and polyimide powder B in a concentration of 1 to 30%, respectively, and then using the solute as a solution. The polyimide A and the polyimide B were mixed so that the weight ratio of the polyimide A/polyimide B=10/90 to 90/10, and produced.

1. 原料 1.1. 芳香族二胺化合物   作為本發明之聚醯亞胺粉體的製造所使用之芳香族二胺化合物,若為可藉由與配合使用之四羧酸二酐的反應,給予可溶於溶媒(例如N,N-二甲基乙醯胺(DMAC))之聚醯亞胺的芳香族二胺化合物,可使用任意之芳香族二胺化合物。具體而言,可列舉m-苯二胺、p-苯二胺、3,4’-二胺基二苯醚、4,4’-二胺基二苯醚、3,3’-二胺基二苯硫醚、3,4’-二胺基二苯硫醚、4,4’-二胺基二苯硫醚、3,3’-二胺基二苯基碸、3,4’-二胺基二苯基碸、4,4’-二胺基二苯基碸、3,3’-二胺基二苯甲酮、3,3’-二胺基二苯基甲烷、3,4’-二胺基二苯基甲烷、4,4’-二胺基二苯基甲烷、2,2-雙(4-胺基苯基)丙烷、2,2-雙(3-胺基苯基)丙烷、2-(3-胺基苯基)-2-(4-胺基苯基)丙烷、2,2-雙(4-胺基苯基)-1,1,1,3,3,3-六氟丙烷、2,2-雙(3-胺基苯基)-1,1,1,3,3,3-六氟丙烷、2-(3-胺基苯基)-2-(4-胺基苯基)-1,1,1,3,3,3-六氟丙烷、1,3-雙(3-胺基苯氧基)苯、1,3-雙(4-胺基苯氧基)苯、1,4-雙(3-胺基苯氧基)苯、1,4-雙(4-胺基苯氧基)苯、4,4’-雙(4-胺基苯氧基)聯苯基、3,3’-雙(4-胺基苯氧基)聯苯基、3,4’-雙(3-胺基苯氧基)聯苯基、雙[4-(4-胺基苯氧基)苯基]硫化物、雙[3-(4-胺基苯氧基)苯基]硫化物、雙[4-(3-胺基苯氧基)苯基]硫化物、雙[3-(4-胺基苯氧基)苯基]硫化物、雙[3-(3-胺基苯氧基)苯基]硫化物、雙[3-(4-胺基苯氧基)苯基]碸、雙[4-(4-胺基苯基)碸、雙[3-(3-胺基苯氧基)苯基]碸、雙[4-(3-胺基苯基)碸、雙[4-(3-胺基苯氧基)苯基]醚、雙[4-(4-胺基苯氧基)苯基]醚、雙[3-(3-胺基苯氧基)苯基]醚、雙[4-(3-胺基苯氧基)苯基]甲烷、雙[4-(4-胺基苯氧基)苯基]甲烷、雙[3-(3-胺基苯氧基)苯基]甲烷、雙[3-(4-胺基苯氧基)苯基]甲烷、2,2-雙[4-(3-胺基苯氧基)苯基]丙烷、2,2-雙[4-(4-胺基苯氧基)苯基]丙烷、2,2-雙[3-(3-胺基苯氧基)苯基]丙烷、2,2-雙[4-(3-胺基苯氧基)苯基]-1,1,1,3,3,3-六氟丙烷、2,2-雙[4-(4-胺基苯氧基)苯基]-1,1,1,3,3,3-六氟丙烷、2,2-雙[3-(3-胺基苯氧基)苯基]-1,1,1,3,3,3-六氟丙烷、2,2-雙[3-(4-胺基苯氧基)苯基]-1,1,1,3,3,3-六氟丙烷、1,3-雙[4-(4-胺基-6-三氟甲基苯氧基)-α,α-二甲基苄基]苯、1,3-雙[4-(4-胺基-6-氟甲基苯氧基)-α,α-二甲基苄基]苯、2,2’-二甲基-4,4’-二胺基聯苯基、3,3’-二甲基-4,4’-二胺基聯苯基、3,3’-雙(三氟甲基)-4,4’-二胺基聯苯基、2,2’-雙(三氟甲基)-4,4’-二胺基聯苯基等。此等之芳香族二胺化合物可單獨使用,亦可使用2種類以上之芳香族二胺化合物。而且,從對透明性、耐熱性、溶媒之溶解性的觀點來看,作為較佳之芳香族二胺化合物,可列舉2,2-雙(4-胺基苯基)-1,1,1,3,3,3-六氟丙烷、2,2-雙(3-胺基苯基)-1,1,1,3,3,3-六氟丙烷、2-(3-胺基苯基)-2-(4-胺基苯基)-1,1,1,3,3,3-六氟丙烷、2,2-雙[4-(3-胺基苯氧基)苯基]-1,1,1,3,3,3-六氟丙烷、2,2-雙[4-(4-胺基苯氧基)苯基]-1,1,1,3,3,3-六氟丙烷、2,2-雙[3-(3-胺基苯氧基)苯基]-1,1,1,3,3,3-六氟丙烷、2,2-雙[3-(4-胺基苯氧基)苯基]-1,1,1,3,3,3-六氟丙烷、1,3-雙[4-(4-胺基-6-三氟甲基苯氧基)-α,α-二甲基苄基]苯、3,3’-雙(三氟甲基)-4,4’-二胺基聯苯基、2,2’-雙(三氟甲基)-4,4’-二胺基聯苯基等之具有氟基之芳香族二胺化合物,使用之芳香族二胺化合物的至少1種類較佳為具有氟基之芳香族二胺化合物,特佳為2,2’-雙(三氟甲基)-4,4’-二胺基聯苯基。藉由使用具有氟基之芳香族二胺化合物,使得到對透明性、耐熱性、機械特性、有機溶媒之可溶性變容易。1. Raw materials 1.1. Aromatic diamine compound As the aromatic diamine compound used for the production of the polyimide powder of the present invention, it can be given by the reaction with the tetracarboxylic dianhydride used in combination. As the aromatic diamine compound of polyimide dissolved in a solvent such as N,N-dimethylacetamide (DMAC), any aromatic diamine compound can be used. Specifically, m-phenylenediamine, p-phenylenediamine, 3,4'-diaminodiphenyl ether, 4,4'-diaminodiphenyl ether, 3,3'-diamine group Diphenyl sulfide, 3,4'-diamino diphenyl sulfide, 4,4'-diamino diphenyl sulfide, 3,3'-diamino diphenyl sulfide, 3,4'-diphenyl sulfide Amino diphenyl sulfone, 4,4'-diamino diphenyl sulfone, 3,3'-diamino benzophenone, 3,3'-diamino diphenylmethane, 3,4' -Diaminodiphenylmethane, 4,4'-diaminodiphenylmethane, 2,2-bis(4-aminophenyl)propane, 2,2-bis(3-aminophenyl) Propane, 2-(3-aminophenyl)-2-(4-aminophenyl)propane, 2,2-bis(4-aminophenyl)-1,1,1,3,3,3 - Hexafluoropropane, 2,2-bis(3-aminophenyl)-1,1,1,3,3,3-hexafluoropropane, 2-(3-aminophenyl)-2-(4 -aminophenyl)-1,1,1,3,3,3-hexafluoropropane, 1,3-bis(3-aminophenoxy)benzene, 1,3-bis(4-aminobenzene) oxy)benzene, 1,4-bis(3-aminophenoxy)benzene, 1,4-bis(4-aminophenoxy)benzene, 4,4'-bis(4-aminophenoxy) base) biphenyl, 3,3'-bis(4-aminophenoxy)biphenyl, 3,4'-bis(3-aminophenoxy)biphenyl, bis[4-(4 -aminophenoxy)phenyl]sulfide, bis[3-(4-aminophenoxy)phenyl]sulfide, bis[4-(3-aminophenoxy)phenyl]sulfide , bis[3-(4-aminophenoxy)phenyl]sulfide, bis[3-(3-aminophenoxy)phenyl]sulfide, bis[3-(4-aminophenoxy) base) phenyl] bis[4-(4-aminophenyl) bis[3-(3-aminophenoxy)phenyl] bis[4-(3-aminophenyl) bis[4-(3-aminophenyl) ) bismuth, bis[4-(3-aminophenoxy)phenyl] ether, bis[4-(4-aminophenoxy)phenyl]ether, bis[3-(3-aminophenoxy) base)phenyl]ether, bis[4-(3-aminophenoxy)phenyl]methane, bis[4-(4-aminophenoxy)phenyl]methane, bis[3-(3- Aminophenoxy)phenyl]methane, bis[3-(4-aminophenoxy)phenyl]methane, 2,2-bis[4-(3-aminophenoxy)phenyl]propane , 2,2-bis[4-(4-aminophenoxy)phenyl]propane, 2,2-bis[3-(3-aminophenoxy)phenyl]propane, 2,2-bis [4-(3-Aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoropropane, 2,2-bis[4-(4-aminophenoxy)benzene base]-1,1,1,3,3,3-hexafluoropropane, 2,2-bis[3-(3-aminophenoxy)phenyl]-1,1,1,3,3, 3-Hexafluoropropane, 2,2-bis[3-(4-aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoropropane, 1,3-bis[4 -(4-Amino-6-trifluoromethylphenoxy)-α,α-di Methylbenzyl]benzene, 1,3-bis[4-(4-amino-6-fluoromethylphenoxy)-α,α-dimethylbenzyl]benzene, 2,2'-dimethyl base-4,4'-diaminobiphenyl, 3,3'-dimethyl-4,4'-diaminobiphenyl, 3,3'-bis(trifluoromethyl)-4, 4'-diaminobiphenyl, 2,2'-bis(trifluoromethyl)-4,4'-diaminobiphenyl, etc. These aromatic diamine compounds may be used alone, or two or more kinds of aromatic diamine compounds may be used. Furthermore, from the viewpoint of transparency, heat resistance, and solubility in a solvent, 2,2-bis(4-aminophenyl)-1,1,1,2,2-bis(4-aminophenyl)-1,1,1, 3,3,3-hexafluoropropane, 2,2-bis(3-aminophenyl)-1,1,1,3,3,3-hexafluoropropane, 2-(3-aminophenyl) -2-(4-Aminophenyl)-1,1,1,3,3,3-hexafluoropropane, 2,2-bis[4-(3-aminophenoxy)phenyl]-1 ,1,1,3,3,3-hexafluoropropane, 2,2-bis[4-(4-aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoro Propane, 2,2-bis[3-(3-aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoropropane, 2,2-bis[3-(4- Aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoropropane, 1,3-bis[4-(4-amino-6-trifluoromethylphenoxy) -α,α-Dimethylbenzyl]benzene, 3,3'-bis(trifluoromethyl)-4,4'-diaminobiphenyl, 2,2'-bis(trifluoromethyl) An aromatic diamine compound having a fluorine group such as -4,4'-diaminobiphenyl, and at least one type of the aromatic diamine compound to be used is preferably an aromatic diamine compound having a fluorine group, particularly preferably It is 2,2'-bis(trifluoromethyl)-4,4'-diaminobiphenyl. By using an aromatic diamine compound having a fluorine group, the solubility in transparency, heat resistance, mechanical properties, and organic solvent is facilitated.

1.2. 四羧酸二酐   又,作為本發明之聚醯亞胺粉體的製造所使用之四羧酸二酐,與上述芳香族二胺化合物相同,若為給予可溶於溶媒(例如N,N-二甲基乙醯胺(DMAC))之聚醯亞胺的四羧酸二酐,則可使用任意者,具體而言,例示有4,4’-(1,1,1,3,3,3-六氟丙烷-2,2-二基)二鄰苯二甲酸二酐、苯均四酸二酐、3,3’,4,4’-二苯甲酮四羧酸二酐、1,4-氫醌二苯甲酸酯-3, 3’,4,4’-四羧酸二酐、3,3’,4,4’-聯苯基四羧酸二酐、3,3’,4,4’-二苯基醚四羧酸二酐等。此等之四羧酸二酐可單獨使用,亦可使用二種類以上之四羧酸二酐。而且,從對耐熱性、機械特性、透明性及溶劑之可溶性的觀點來看,較佳為使用4,4’-(1,1,1,3,3,3-六氟丙烷-2,2-二基)二鄰苯二甲酸二酐等具有至少1種類之氟基的四羧酸二酐。1.2. Tetracarboxylic dianhydride Also, as the tetracarboxylic dianhydride used in the production of the polyimide powder of the present invention, it is the same as the above-mentioned aromatic diamine compound, if it is given a soluble solvent (such as N, Any tetracarboxylic dianhydride of polyimide such as N-dimethylacetamide (DMAC)) can be used, and specifically, 4,4'-(1,1,1,3, 3,3-hexafluoropropane-2,2-diyl) diphthalic dianhydride, pyromellitic dianhydride, 3,3',4,4'-benzophenone tetracarboxylic dianhydride, 1,4-hydroquinone dibenzoate-3,3',4,4'-tetracarboxylic dianhydride, 3,3',4,4'-biphenyltetracarboxylic dianhydride, 3,3 ',4,4'-diphenyl ether tetracarboxylic dianhydride, etc. These tetracarboxylic dianhydrides may be used alone, or two or more types of tetracarboxylic dianhydrides may be used. Furthermore, from the viewpoint of heat resistance, mechanical properties, transparency, and solubility in solvents, it is preferable to use 4,4'-(1,1,1,3,3,3-hexafluoropropane-2,2 - Tetracarboxylic dianhydride having at least one type of fluorine group, such as diphthalic dianhydride.

2. 聚醯亞胺粉體的製造方法   本發明之聚醯亞胺粉體可將芳香族二胺化合物及四羧酸二酐作為原料,經由對聚醯胺酸之聚合、醯亞胺化反應、粉體化及乾燥之各步驟製造。2. The manufacturing method of polyimide powder The polyimide powder of the present invention can use aromatic diamine compound and tetracarboxylic dianhydride as raw materials, through the polymerization of polyimide, and the imidization reaction , powdering and drying steps.

2.1. 對聚醯胺酸之聚合   對聚醯胺酸之聚合可藉由於對可溶生成之聚醯胺酸的溶劑之溶解下,使上述芳香族二胺化合物及四羧酸二酐進行反應來進行。作為對聚醯胺酸之聚合所使用之溶劑,可使用N,N-二甲基乙醯胺、N,N-二甲基甲醯胺、N-甲基-2-吡咯烷酮、1,3-二甲基-2-四氫咪唑酮、二甲基亞碸等之溶劑。2.1. Polymerization of polyamic acid The polymerization of polyamic acid can be obtained by reacting the above-mentioned aromatic diamine compound and tetracarboxylic dianhydride by dissolving the solvent in which the polyamic acid is soluble. conduct. As the solvent used for the polymerization of p-polyamic acid, N,N-dimethylacetamide, N,N-dimethylformamide, N-methyl-2-pyrrolidone, 1,3- Solvents for dimethyl-2-tetrahydroimidazolone, dimethyl sulfoxide, etc.

對聚醯胺酸之聚合反應較佳為以具備攪拌裝置之反應容器邊攪拌邊進行。例如可列舉於上述溶劑使指定量之芳香族二胺化合物溶解,邊攪拌邊投入四羧酸二酐,進行反應而得到聚醯胺酸之方法、使四羧酸二酐溶解在溶劑,邊攪拌邊投入芳香族二胺化合物,進行反應而得到聚醯胺酸之方法、交替投入芳香族二胺化合物與四羧酸二酐進行反應,而得到聚醯胺酸之方法等。The polymerization reaction of the polyamic acid is preferably carried out while stirring in a reaction vessel equipped with a stirring device. For example, a method of dissolving a predetermined amount of an aromatic diamine compound in the above-mentioned solvent, adding tetracarboxylic dianhydride while stirring, and reacting to obtain a polyamic acid can be exemplified. The method of dissolving tetracarboxylic dianhydride in the solvent and stirring A method of obtaining a polyamic acid while adding an aromatic diamine compound and reacting, a method of alternately adding an aromatic diamine compound and a tetracarboxylic dianhydride and reacting to obtain a polyamic acid, etc.

針對對聚醯胺酸之聚合反應的溫度雖並未特別制約,但較佳為以0~70℃的溫度進行,更佳為10~60℃,再更佳為20~50℃。藉由將聚合反應於上述範圍內進行,可得到著色少且透明性優異之聚醯胺酸。The temperature for the polymerization reaction of the polyamic acid is not particularly limited, but it is preferably carried out at a temperature of 0 to 70°C, more preferably 10 to 60°C, and even more preferably 20 to 50°C. By carrying out the polymerization reaction within the above-mentioned range, a polyamic acid having little coloration and excellent transparency can be obtained.

又,對聚醯胺酸之聚合所使用之芳香族二胺化合物與四羧酸二酐雖大致使用當莫耳量,但為了控制所得之聚醯胺酸的聚合度,得到指定之還原黏度或重量平均分子量的聚醯亞胺,亦可使四羧酸二酐的莫耳量/芳香族二胺化合物的莫耳量(莫耳比率)於0.95~1.05的範圍變化。而且,為了聚合給予還原黏度為1.2dL/g以上且未滿2.1dL/g或是重量平均分子量為100,000g/mol以上且未滿250,000g/mol,或還原黏度為2.1dL/g以上3.0dL/g以下或是重量平均分子量為250,000g/mol以上500,000g/mol以下之聚醯亞胺的聚醯胺酸,良好地控制四羧酸與芳香族二胺化合物的莫耳比率或溶媒中之水分量等來製造為重要。四羧酸二酐與芳香族二胺化合物的莫耳比率較佳為1.001~1.02的範圍,更佳為1.002~1.015。如此藉由僅過剩四羧酸二酐些微,可使所得之聚醯胺酸的聚合度安定,並且可將源自四羧酸二酐的單位配置在聚合物的末端,其結果,變成可給予著色少且透明性優異之聚醯亞胺。In addition, although the aromatic diamine compound and tetracarboxylic dianhydride used in the polymerization of the polyamic acid are roughly used in molar amounts, in order to control the polymerization degree of the obtained polyamic acid, a specified reduction viscosity or The polyimide of the weight average molecular weight can also change the molar amount of the tetracarboxylic dianhydride/the molar amount (molar ratio) of the aromatic diamine compound within the range of 0.95 to 1.05. Furthermore, for polymerization, the reduced viscosity is 1.2 dL/g or more and less than 2.1 dL/g, the weight average molecular weight is 100,000 g/mol or more and less than 250,000 g/mol, or the reduced viscosity is 2.1 dL/g or more and 3.0 dL /g or less, or polyamide acid with a weight-average molecular weight of 250,000 g/mol or more and 500,000 g/mol or less of polyimide, the molar ratio of the tetracarboxylic acid and the aromatic diamine compound or the ratio in the solvent is well controlled. It is important to manufacture with moisture content etc. The molar ratio of the tetracarboxylic dianhydride to the aromatic diamine compound is preferably in the range of 1.001 to 1.02, more preferably 1.002 to 1.015. In this way, the degree of polymerization of the obtained polyamic acid can be stabilized by only a little excess of tetracarboxylic dianhydride, and the unit derived from tetracarboxylic dianhydride can be arranged at the end of the polymer, as a result, it becomes possible to give Polyimide with little coloration and excellent transparency.

較佳為生成之聚醯胺酸溶液的濃度適當保持溶液的黏度,以於之後的步驟的操作變容易的方式,調整在適當的濃度(例如10~30重量%左右)。It is preferable that the concentration of the resulting polyamic acid solution maintains the viscosity of the solution appropriately, and is adjusted to an appropriate concentration (for example, about 10 to 30 wt %) so as to facilitate the operation in the subsequent steps.

2.2. 醯亞胺化反應   醯亞胺化以下所得之聚醯胺酸溶液中之聚醯胺酸。醯亞胺化可藉由加熱聚醯胺酸溶液進行熱醯亞胺化,或使用醯亞胺化劑進行化學醯亞胺化等來進行。而且,從所得之聚醯亞胺的還原黏度或重量平均分子量的控制的容易性,或得到良好之耐熱性、機械特性及透明性等之聚醯亞胺的特性的觀點來看,較佳為藉由化學醯亞胺化之醯亞胺化。作為化學醯亞胺化反應所使用之醯亞胺化劑,可使用乙酸酐、丙酸酐、琥珀酸酐、鄰苯二甲酸酐、苯甲酸酐等之羧酸酐,從成本或反應後之去除的容易性的觀點來看,較佳為使用乙酸酐。使用之醯亞胺化劑的當量為進行化學醯亞胺化反應之聚醯胺酸的醯胺鍵的當量以上,較佳為醯胺鍵之當量的1.1~5倍,更佳為1.5~4倍。如此對於醯胺鍵,藉由使用少許過剩之醯亞胺化劑,即使比較低溫亦可有效率地進行醯亞胺化反應。2.2. Imidization reaction The polyamic acid in the polyamic acid solution obtained below was imidized. The imidization can be performed by thermal imidization by heating a polyimide solution, or chemical imidization using an imidizing agent, or the like. In addition, from the viewpoint of the ease of control of the reduced viscosity or weight average molecular weight of the obtained polyimide, or from the viewpoint of obtaining the characteristics of the polyimide such as good heat resistance, mechanical properties, and transparency, it is preferably Imidization by chemical imidization. As the imidizing agent used in the chemical imidization reaction, carboxylic anhydrides such as acetic anhydride, propionic anhydride, succinic anhydride, phthalic anhydride, benzoic anhydride, etc. can be used, which are easy to remove from cost and after the reaction. From the viewpoint of properties, acetic anhydride is preferably used. The equivalent of the imidizing agent to be used is more than the equivalent of the amide bond of the polyamic acid for chemical imidization, preferably 1.1 to 5 times the equivalent of the amide bond, more preferably 1.5 to 4 times. As described above, the imidization reaction can be efficiently performed even at a relatively low temperature by using a small excess of the imidization agent for the imide bond.

又,化學醯亞胺化反應中,作為醯亞胺化促進劑,可使用吡啶、甲吡啶(Picoline)、喹啉、異喹啉、三甲基胺、三乙基胺等之脂肪族、芳香族或雜環式第三級胺類。藉由使用這般的胺類,可低溫且有效率地進行醯亞胺化反應,其結果使抑制醯亞胺化反應時之著色變可能,可得到更透明之聚醯亞胺。In addition, in the chemical imidization reaction, as the imidization accelerator, aliphatic and aromatic such as pyridine, picoline, quinoline, isoquinoline, trimethylamine, and triethylamine can be used. family or heterocyclic tertiary amines. By using such amines, the imidization reaction can be carried out efficiently at a low temperature, and as a result, it becomes possible to suppress the coloration during the imidization reaction, and a more transparent polyimide can be obtained.

對於化學醯亞胺化反應溫度雖並未特別制約,但較佳為於10℃以上且未滿50℃進行,更佳為於15℃以上且未滿45℃進行。藉由於10℃以上且未滿50℃的溫度進行化學醯亞胺化反應,抑制醯亞胺化前之聚醯胺酸的分裂,使還原黏度或重量平均分子量的控制變容易,並且抑制聚醯亞胺的著色,可得到透明性優異之聚醯亞胺。Although the chemical imidization reaction temperature is not particularly limited, it is preferably 10°C or higher and lower than 50°C, more preferably 15°C or higher and lower than 45°C. By carrying out the chemical imidization reaction at a temperature of 10°C or more and less than 50°C, the cleavage of the polyimide before imidization is suppressed, the control of the reduction viscosity or the weight average molecular weight is facilitated, and the polyimide is suppressed. The coloration of imine can obtain polyimide with excellent transparency.

2.3. 粉體化   接著進行藉由醯亞胺化所得之聚醯亞胺溶液中之聚醯亞胺的粉體化。聚醯亞胺之粉體化雖可用任意之方法進行,但加入聚醯亞胺之貧溶媒使聚醯亞胺析出,形成粉體之方法簡便故較佳。加入貧溶媒進行聚醯亞胺之析出暨粉體化時,作為貧溶媒,可使用可析出聚醯亞胺之任意貧溶媒,所謂聚醯亞胺溶液的溶媒由於期望混和性,故具體而言,可使用水、甲醇、乙醇等。而且,藉由使用甲醇作為貧溶媒,可收率良好地得到安定之形狀的聚醯亞胺粉體故較佳。2.3. Powderization Next, powderization of the polyimide in the polyimide solution obtained by imidization is performed. Although the powdering of polyimide can be carried out by any method, adding a poor solvent of polyimide to precipitate the polyimide and forming the powder is preferable because the method is simple. When a poor solvent is added for the precipitation and powdering of polyimide, as the poor solvent, any poor solvent that can precipitate polyimide can be used. The solvent of the so-called polyimide solution is expected to be miscible, so specifically , water, methanol, ethanol, etc. can be used. Furthermore, by using methanol as a poor solvent, it is preferable that a stable polyimide powder can be obtained in a good yield.

進行藉由貧溶媒之聚醯亞胺的析出暨粉體化時,使用之貧溶媒的量為了進行聚醯亞胺的析出粉體化有必要投入充分的量,雖考量聚醯亞胺的構造、聚醯亞胺溶液的溶媒、聚醯亞胺的溶液濃度等來決定,但通常為使用聚醯亞胺溶液重量的0.5倍以上,較佳為聚醯亞胺溶液重量的0.8倍以上,更佳為聚醯亞胺溶液重量的1倍以上之重量的貧溶媒。將聚醯亞胺溶液藉由使用重量的0.5倍以上之重量的貧溶媒,可高收率得到安定之形狀的聚醯亞胺粉體。又,通常為使用聚醯亞胺溶液重量的10倍以下,較佳為聚醯亞胺溶液重量的7倍以下,更佳為聚醯亞胺溶液重量的5倍以下,再更佳為聚醯亞胺溶液重量的4倍以下之重量的貧溶媒。When performing precipitation and powdering of polyimide by a poor solvent, the amount of the poor solvent to be used must be sufficient for precipitation and powdering of polyimide, although the structure of polyimide is considered. , the solvent of the polyimide solution, the concentration of the polyimide solution, etc., but usually it is more than 0.5 times the weight of the polyimide solution used, preferably more than 0.8 times the weight of the polyimide solution, more Preferably, it is a lean solvent in a weight of 1 times or more the weight of the polyimide solution. The polyimide powder in a stable shape can be obtained in a high yield by using a lean solvent of 0.5 times or more the weight of the polyimide solution. In addition, it is usually 10 times or less the weight of the polyimide solution used, preferably 7 times or less the weight of the polyimide solution, more preferably 5 times or less the weight of the polyimide solution, and still more preferably the polyimide solution. A lean solvent with a weight of 4 times or less the weight of the imine solution.

將聚醯亞胺的粉體化如上述,藉由於聚醯亞胺溶液添加貧溶媒來進行時,較佳為以邊攪拌聚醯亞胺溶液,邊滴下貧溶媒的方法進行。為了使貧溶媒的擴散變容易,聚醯亞胺溶液期望預先調整至較佳為5~30重量%,更佳為10~20重量%左右的濃度。又,藉由本發明所得之聚醯亞胺粉體的較佳之平均粒徑雖為0.02~0.8mm,但平均粒徑可藉由對聚醯亞胺溶液之貧溶媒的添加速度來控制。When the powdering of the polyimide is carried out by adding a poor solvent to the polyimide solution as described above, it is preferably carried out by a method of dropping the poor solvent while stirring the polyimide solution. In order to facilitate the diffusion of the poor solvent, the polyimide solution is desirably adjusted to a concentration of preferably about 5 to 30% by weight, more preferably about 10 to 20% by weight. In addition, although the preferred average particle size of the polyimide powder obtained by the present invention is 0.02-0.8 mm, the average particle size can be controlled by the addition rate of the poor solvent to the polyimide solution.

在本發明,聚醯亞胺之粉體化的溫度雖並未特別制約,但藉由貧溶媒的添加進行析出暨粉體化時,從抑制貧溶媒的蒸發,有效率地進行析出的觀點來看,較佳為於50℃以下之溫度進行,更佳為於40℃以下進行。In the present invention, the temperature for powdering polyimide is not particularly limited, but when precipitation and powdering are performed by adding a poor solvent, the evaporation of the poor solvent is suppressed and the precipitation is efficiently performed. See, it is preferable to carry out at the temperature of 50 degrees C or less, and it is more preferable to carry out at 40 degrees C or less.

2.4. 乾燥   進行以下所得之聚醯亞胺粉體的乾燥,去除溶媒、醯亞胺化劑、醯亞胺化促進劑、貧溶媒等。乾燥係藉由將聚醯亞胺粉體預先由過濾裝置進行濾除,進而如有必要進行洗淨,於提前去除上述聚醯亞胺的溶媒、醯亞胺化劑、醯亞胺化促進劑後進行,以有效率地進行乾燥來看較佳。2.4. Drying The polyimide powder obtained below is dried to remove the solvent, imidization agent, imidization accelerator, poor solvent, etc. The drying system removes the above-mentioned polyimide solvent, imidization agent, and imidization accelerator in advance by filtering the polyimide powder through a filter device in advance, and then washing it if necessary. It is preferable to carry out the drying later, in view of efficient drying.

上述聚醯亞胺粉體的乾燥,若為可去除聚醯亞胺溶媒、醯亞胺化劑、醯亞胺化促進劑、貧溶媒等之殘渣,雖可於任意之溫度進行,但例如於上述貧溶媒使用具有甲醇、乙醇等之羥基的貧溶媒時,馬上以100℃以上的溫度進行乾燥時,有聚醯亞胺中之羧酸基或羧酸酐基與上述貧溶媒進行反應,導致生成酯鍵,引起耐熱性的降低、著色進一步引進分子量的降低的問題的可能性。據此,乾燥步驟較佳為從未滿100℃的溫度與100~350℃的溫度之2階段以上,或從未滿100℃的溫度,昇溫至100℃以上350℃以下的溫度來進行。又,聚醯亞胺粉體的乾燥可於常壓進行,即使於減壓下進行亦沒問題。The drying of the above-mentioned polyimide powder can be carried out at any temperature if it can remove the residues of the polyimide solvent, imidization agent, imidization accelerator, poor solvent, etc. When a poor solvent having hydroxyl groups such as methanol and ethanol is used as the above-mentioned poor solvent, and immediately drying at a temperature of 100°C or higher, the carboxylic acid group or carboxylic acid anhydride group in the polyimide reacts with the above-mentioned poor solvent, resulting in the formation of The ester bond may cause a decrease in heat resistance, and coloration may further introduce the problem of a decrease in molecular weight. Accordingly, the drying step is preferably performed in two stages or more from a temperature below 100°C and a temperature from 100 to 350°C, or from a temperature below 100°C to a temperature from 100°C to 350°C. In addition, the drying of the polyimide powder can be performed under normal pressure, and there is no problem even if it is performed under reduced pressure.

3. 聚醯亞胺粉體   本發明之第一實施態樣之聚醯亞胺粉體,可藉由將聚醯亞胺粉體A、與聚醯亞胺粉體B以重量比率,以成為聚醯亞胺粉體A/聚醯亞胺粉體B=10/90~90/10的方式進行混合,將對於所得之混合所測定之還原黏度調整成1.7~2.5dL/g,較佳為1.8~2.4dL/g,更佳為1.9~2.3dL/g,特佳為2.0~2.2dL/g,或將對於所得之混合所測定之重量平均分子量調整成160,000~350,000g/mol,較佳為200,000~330,000g/mol,更佳為220,000~310,000g/mol,特佳為240,000~290,000g/mol而得到,而該聚醯亞胺粉體A係由藉由上述方法所得之(a-1)還原黏度為1.2dL/g以上且未滿2.1dL/g,較佳為1.4dL/g以上且未滿2.1dL/g之聚醯亞胺,或(a-2)重量平均分子量為100,000g/mol以上且未滿250,000g/mol,較佳為150,000g/mol以上且未滿250,000 g/mol之聚醯亞胺所構成,該聚醯亞胺粉體B係由(b-1)還原黏度為2.1dL/g以上3.0dL/g以下,較佳為2.1dL/g以上2.8dL/g以下之聚醯亞胺,或(b-2)重量平均分子量為250,000g/mol以上500,000g/mol以下,較佳為250,000g/mol以上400,000g/mol以下之聚醯亞胺所構成。3. Polyimide Powder The polyimide powder of the first embodiment of the present invention can be obtained by mixing the polyimide powder A and the polyimide powder B in a weight ratio. Mix the polyimide powder A/polyimide powder B=10/90 to 90/10, and adjust the reduced viscosity measured for the resulting mixture to 1.7 to 2.5 dL/g, preferably 1.8~2.4dL/g, more preferably 1.9~2.3dL/g, particularly preferably 2.0~2.2dL/g, or the weight average molecular weight measured for the obtained mixture is adjusted to 160,000~350,000g/mol, preferably 200,000-330,000 g/mol, more preferably 220,000-310,000 g/mol, particularly preferably 240,000-290,000 g/mol, and the polyimide powder A is obtained by the above-mentioned method (a- 1) Polyimide with reduced viscosity of 1.2dL/g or more and less than 2.1dL/g, preferably 1.4dL/g or more and less than 2.1dL/g, or (a-2) Weight average molecular weight of 100,000 g/mol or more and less than 250,000 g/mol, preferably 150,000 g/mol or more and less than 250,000 g/mol of polyimide, the polyimide powder B is composed of (b-1) Polyimide with reduced viscosity of 2.1dL/g or more and 3.0dL/g or less, preferably 2.1dL/g or more and 2.8dL/g or less, or (b-2) weight average molecular weight of 250,000g/mol or more and 500,000g /mol or less, preferably 250,000 g/mol or more and 400,000 g/mol or less of polyimide.

聚醯亞胺粉體的混合,例如可以使用回轉型混合機之方法、使用水平式攪拌型混合機之方法、使用垂直式攪拌型混合機之方法等,可均一混合聚醯亞胺粉體A與聚醯亞胺粉體B的任意方法進行。For the mixing of the polyimide powder, for example, the method of using a rotary mixer, the method of using a horizontal stirring mixer, the method of using a vertical stirring mixer, etc., can be used to uniformly mix the polyimide powder A. It is carried out by any method with polyimide powder B.

4. 聚醯亞胺塗料   本發明之第二實施態樣之聚醯亞胺塗料,可藉由將聚醯亞胺粉體於可溶聚醯亞胺之任意有機溶媒以1~30重量%的濃度溶解而得到,該聚醯亞胺粉體係將上述聚醯亞胺粉體A與聚醯亞胺粉體B,以指定的重量比率進行混合所得之呈現第一實施態樣之還原黏度1.7~2.5dL/g,或重量平均分子量160,000~350,000g/mol。4. Polyimide coating The polyimide coating of the second embodiment of the present invention can be prepared by mixing the polyimide powder in any organic solvent soluble in polyimide at a concentration of 1 to 30 wt %. The polyimide powder system is obtained by dissolving the above-mentioned polyimide powder A and polyimide powder B at a specified weight ratio, and the reduced viscosity of the first embodiment is 1.7~ 2.5dL/g, or a weight average molecular weight of 160,000 to 350,000 g/mol.

又,本發明之聚醯亞胺塗料亦可於將前述聚醯亞胺粉體A與聚醯亞胺粉體B以粉體的狀態進行混合之前,分別於有機溶媒以1~30重量%的濃度溶解作為聚醯亞胺溶液後,使溶質之聚醯亞胺A與聚醯亞胺B的重量比率成為10/90~90/10的範圍的方式,混合個別的聚醯亞胺溶液成為作為目的之聚醯亞胺塗料。In addition, the polyimide coating of the present invention can also be mixed in an organic solvent with 1 to 30% by weight of the polyimide powder A and the polyimide powder B in the powder state. After the concentration is dissolved as the polyimide solution, the weight ratio of the polyimide A and the polyimide B as the solute is in the range of 10/90 to 90/10, and the individual polyimide solutions are mixed to become the polyimide solution. The purpose of the polyimide coating.

5. 聚醯亞胺特性(其1 粉體特性)   構成混合前之聚醯亞胺粉體A之聚醯亞胺的還原黏度為1.2dL/g以上且未滿2.1dL/g,構成聚醯亞胺粉體B之聚醯亞胺的還原黏度為2.1dL/g以上3.0dL/g以下,對於混合聚醯亞胺粉體A與聚醯亞胺粉體B後之本發明之第一實施態樣的聚醯亞胺粉體所測定之還原黏度為1.7~2.5dL/g,較佳為1.8~2.4dL/g,更佳為1.9~2.3dL/g,特佳為2.0~2.2dL/g。對於聚醯亞胺粉體所測定之還原黏度未滿1.7dL/g時,損害最終所得之聚醯亞胺薄膜的拉伸強度伸長度及耐彎曲性等之機械特性,並且對聚醯亞胺之吸濕有增大之虞,還原黏度超過2.5dL/g時,聚醯亞胺溶液的黏度過高,產生進行操作變困難的問題。5. Polyimide Properties (1 Powder Properties) The reduction viscosity of the polyimide constituting the polyimide powder A before mixing is 1.2 dL/g or more and less than 2.1 dL/g, which constitutes the polyimide The reducing viscosity of the polyimide of the imine powder B is 2.1 dL/g or more and 3.0 dL/g or less. For the first implementation of the present invention after mixing the polyimide powder A and the polyimide powder B The measured reducing viscosity of the polyimide powder of this embodiment is 1.7-2.5dL/g, preferably 1.8-2.4dL/g, more preferably 1.9-2.3dL/g, particularly preferably 2.0-2.2dL/g g. When the reduced viscosity measured for the polyimide powder is less than 1.7 dL/g, the mechanical properties such as the tensile strength, elongation, and bending resistance of the finally obtained polyimide film are impaired, and the polyimide The hygroscopicity may increase, and when the reduced viscosity exceeds 2.5 dL/g, the viscosity of the polyimide solution is too high, resulting in a problem that handling becomes difficult.

又,在本發明,藉由混合由低還原黏度之聚醯亞胺所構成之聚醯亞胺粉體A與由高還原黏度之聚醯亞胺所構成之聚醯亞胺粉體B,具有混合後之聚醯亞胺所呈現之還原黏度的控制變容易,並且所得之聚醯亞胺薄膜的機械特性,顯示有較由未進行混合之聚醯亞胺粉體所得之聚醯亞胺薄膜的機械特性更優異之傾向的優點。Furthermore, in the present invention, by mixing the polyimide powder A composed of the polyimide with a low reduction viscosity and the polyimide powder B composed of the polyimide with a high reduction viscosity, the The control of the reduced viscosity of the mixed polyimide becomes easier, and the mechanical properties of the obtained polyimide film are better than those obtained from the unmixed polyimide powder. The advantage of the tendency to have more excellent mechanical properties.

或構成混合前之聚醯亞胺粉體A之聚醯亞胺的重量平均分子量為100,000g/mol以上且未滿250,000 g/mol,構成聚醯亞胺粉體B之聚醯亞胺的重量平均分子量為250,000g/mol以上500,000g/mol以下,對於混合聚醯亞胺粉體A與聚醯亞胺粉體B後之本發明之第一實施態樣的聚醯亞胺粉體所測定之重量平均分子量為160,000~350,000g/mol,較佳為200,000~330,000g/mol,更佳為220,000~310,000g/mol,特佳為240,000~290,000g/mol。對於聚醯亞胺粉體所測定之重量平均分子量未滿160,000g/mol時,損害最終所得之聚醯亞胺薄膜的拉伸強度伸長度及耐彎曲性等之機械特性,並且對聚醯亞胺之吸濕有增大之虞,重量平均分子量超過350,000g/mol時,聚醯亞胺溶液的黏度過高,產生進行操作變困難的問題。Or the weight average molecular weight of the polyimide constituting the polyimide powder A before mixing is 100,000 g/mol or more and less than 250,000 g/mol, and the weight of the polyimide constituting the polyimide powder B The average molecular weight is 250,000 g/mol or more and 500,000 g/mol or less, measured on the polyimide powder of the first embodiment of the present invention after mixing the polyimide powder A and the polyimide powder B The weight average molecular weight is 160,000-350,000 g/mol, preferably 200,000-330,000 g/mol, more preferably 220,000-310,000 g/mol, particularly preferably 240,000-290,000 g/mol. When the weight-average molecular weight measured for the polyimide powder is less than 160,000 g/mol, the mechanical properties such as tensile strength, elongation, and bending resistance of the final polyimide film are impaired, and the polyimide film is not suitable for polyimide. There is a possibility that the moisture absorption of the amine may increase, and when the weight average molecular weight exceeds 350,000 g/mol, the viscosity of the polyimide solution is too high, and there is a problem that handling becomes difficult.

又,在本發明,藉由混合由低重量平均分子量之聚醯亞胺所構成之聚醯亞胺粉體A與由高重量平均分子量之聚醯亞胺所構成之聚醯亞胺粉體B,具有顯示混合後之聚醯亞胺所呈現之重量平均分子量的控制變容易,並且所得之聚醯亞胺薄膜的機械特性,較由未進行混合之聚醯亞胺粉體所得之聚醯亞胺薄膜的機械特性更優異之傾向的優點。Moreover, in the present invention, by mixing the polyimide powder A composed of the low weight average molecular weight polyimide and the polyimide powder B composed of the high weight average molecular weight polyimide , it is easy to control the weight average molecular weight exhibited by the mixed polyimide, and the mechanical properties of the obtained polyimide film are better than those obtained from the unmixed polyimide powder. It is an advantage of the tendency that the mechanical properties of the amine film are more excellent.

又,聚醯亞胺粉體之平均粒徑較佳為0.02~0.8mm,更佳為0.03~0.6mm。若平均粒徑為0.02~0.8mm的範圍,有效率地去除聚醯亞胺粉體中之溶媒、貧溶媒、醯亞胺化劑等之殘存揮發成分,易得到著色極為少且透明性優異之聚醯亞胺。Moreover, the average particle diameter of the polyimide powder is preferably 0.02 to 0.8 mm, more preferably 0.03 to 0.6 mm. If the average particle size is in the range of 0.02 to 0.8 mm, residual volatile components such as solvent, poor solvent, imidizing agent, etc. in the polyimide powder can be efficiently removed, and it is easy to obtain a product with very little coloration and excellent transparency. Polyimide.

本發明之聚醯亞胺粉體的平均粒徑可藉由雷射繞射/散射式粒徑分布測定裝置測定。The average particle size of the polyimide powder of the present invention can be measured by a laser diffraction/scattering particle size distribution analyzer.

7. 聚醯亞胺特性(其2 塗料特性)   本發明之第二實施態樣的聚醯亞胺塗料,可將聚醯亞胺粉體A與聚醯亞胺粉體B以聚醯亞胺粉體A/聚醯亞胺粉體B的重量比率以10/90~90/10的範圍進行混合所得之本發明之第一實施態樣即聚醯亞胺粉體,以成為1~30重量份的濃度的方式溶解在有機溶媒而得到,該聚醯亞胺粉體A係由還原黏度為1.2dL/g以上且未滿2.1dL/g之聚醯亞胺所構成,該聚醯亞胺粉體B係由還原黏度為2.1dL/g以上3.0dL/g以下之聚醯亞胺所構成。7. Polyimide Properties (2 Coating Properties) In the polyimide coating of the second embodiment of the present invention, the polyimide powder A and the polyimide powder B can be mixed with polyimide. The weight ratio of powder A/polyimide powder B is mixed in the range of 10/90 to 90/10, that is, the polyimide powder, which is the first embodiment of the present invention, is 1 to 30 by weight. The polyimide powder A is obtained by dissolving it in an organic solvent so that the concentration of Powder B is composed of polyimide having a reduced viscosity of not less than 2.1 dL/g and not more than 3.0 dL/g.

或本發明之第二實施態樣的聚醯亞胺塗料,可將聚醯亞胺粉體A與聚醯亞胺粉體B以聚醯亞胺粉體A/聚醯亞胺粉體B的重量比率以10/90~90/10的範圍進行混合所得之本發明之第一實施態樣即聚醯亞胺粉體,以成為1~30重量份的濃度的方式溶解在有機溶媒而得到,該聚醯亞胺粉體A係由重量平均分子量為100,000g/mol以上且未滿250,000g/mol之聚醯亞胺所構成,該聚醯亞胺粉體B係由重量平均分子量為250,000g/mol以上500,000g/mol以下之聚醯亞胺所構成。Or in the polyimide coating of the second embodiment of the present invention, the polyimide powder A and the polyimide powder B can be mixed with the polyimide powder A/polyimide powder B. The polyimide powder, which is the first embodiment of the present invention obtained by mixing the weight ratio in the range of 10/90 to 90/10, is obtained by dissolving it in an organic solvent so as to have a concentration of 1 to 30 parts by weight, The polyimide powder A is composed of polyimide with a weight average molecular weight of 100,000 g/mol or more and less than 250,000 g/mol, and the polyimide powder B is composed of a weight average molecular weight of 250,000 g /mol or more and 500,000 g/mol or less of polyimide.

又,本發明之聚醯亞胺塗料亦可將聚醯亞胺粉體A以成為1~30重量%的濃度的方式溶解在有機溶媒的塗料、與將聚醯亞胺粉體B以成為1~30重量%的濃度的方式溶解在有機溶媒的塗料,以溶解中之聚醯亞胺粉體A與聚醯亞胺粉體B的重量比成為A/B=10/90~90/10的方式進行混合而得到。In addition, the polyimide paint of the present invention may be a paint in which the polyimide powder A is dissolved in an organic solvent at a concentration of 1 to 30% by weight, and the polyimide powder B may be 1 The paint is dissolved in an organic solvent at a concentration of ~30% by weight, and the weight ratio of the polyimide powder A and the polyimide powder B in solution is A/B=10/90~90/10 obtained by mixing.

本發明之聚醯亞胺塗料所使用之有機溶媒,若為可溶解聚醯亞胺粉體之有機溶媒,則可為任意之溶媒,可適合使用N,N-二甲基乙醯胺、N,N-二甲基甲醯胺、N-甲基-2-吡咯烷酮、γ-丁內酯、2-丁酮、乙腈等。又,本發明之聚醯亞胺塗料所使用之有機溶媒可單獨使用,亦可混合2種類以上亦沒問題,若混合2種類以上之溶媒時,混合之溶媒若為可溶解聚醯亞胺粉體則無妨。又,若可維持溶解性,即使包含水等之有機溶媒以外的成分亦無妨。The organic solvent used in the polyimide coating of the present invention can be any solvent if it can dissolve the polyimide powder, and N,N-dimethylacetamide, N , N-dimethylformamide, N-methyl-2-pyrrolidone, γ-butyrolactone, 2-butanone, acetonitrile, etc. In addition, the organic solvent used in the polyimide paint of the present invention can be used alone, or it can be mixed with two or more kinds of solvents. The body is fine. Moreover, as long as solubility can be maintained, even if it contains components other than organic solvents, such as water, it does not matter.

8. 聚醯亞胺特性(其3 薄膜特性)   針對本發明之聚醯亞胺粉體或聚醯亞胺塗料中聚醯亞胺的透明性,可將聚醯亞胺粉體溶解在N,N-二甲基乙醯胺(DMAC)而成為聚醯亞胺塗料後,使用以乾燥後成為50μm厚度的方式藉由澆鑄法進行製膜之薄膜,藉由分光色彩計所測定之全光線透過率及藉由黃色度求出。而且,由本發明之聚醯亞胺粉體或聚醯亞胺塗料所得之聚醯亞胺薄膜的全光線透過率較佳為85%以上,更佳為90%以上。又,針對黃色度,較佳為-3~3,更佳為-2~2,再更佳為-1.5~1.5。全光線透過率未滿上述之下限時或黃色度為上述範圍外時,有給予可使用在顯示器等之光學用途之透明性優異的薄膜變困難的情況。又,構成本發明之聚醯亞胺粉體之聚醯亞胺的醯亞胺化率較佳為90%以上,更佳為95%以上。醯亞胺化率可藉由由上述方法所得之聚醯亞胺薄膜的傅立葉變換紅外分光法(FT-IR法)求出。 [實施例]8. Polyimide properties (3 film properties) For the transparency of the polyimide powder or polyimide coating of the present invention, the polyimide powder can be dissolved in N, After using N-dimethylacetamide (DMAC) as a polyimide coating, a film formed by a casting method so as to have a thickness of 50 μm after drying was used, and the total light transmission measured by a spectrocolorimeter was used. rate and obtained by yellowness. Furthermore, the total light transmittance of the polyimide film obtained from the polyimide powder or polyimide coating of the present invention is preferably 85% or more, more preferably 90% or more. Moreover, it is preferable that it is -3 to 3, it is more preferable that it is -2 to 2, and it is still more preferable that it is -1.5 to 1.5 with respect to yellowness. When the total light transmittance is less than the above lower limit, or when the yellowness is outside the above range, it may be difficult to provide a film having excellent transparency for use in optical applications such as displays. Moreover, the imidization rate of the polyimide constituting the polyimide powder of the present invention is preferably 90% or more, more preferably 95% or more. The imidization rate can be determined by Fourier transform infrared spectroscopy (FT-IR method) of the polyimide film obtained by the above method. [Example]

以下,雖由實施例具體說明本發明,但本發明並非被限定於此等實施例者。Hereinafter, the present invention will be specifically described by way of examples, but the present invention is not limited to these examples.

(聚醯亞胺之還原黏度的測定方法)   作成以成為0.5g/dL的濃度的方式於N,N-二甲基乙醯胺(DMAC)溶解聚醯亞胺粉體之聚醯亞胺溶液。使用烏氏黏度計,測定於30℃的溫度聚醯亞胺溶液的流出時間(T)與於僅溶媒之DMAC的流出時間(T0),由下述之式求出還原黏度。   還原黏度(dL/g)=(T-T0)/T0/0.5(Method for measuring the reduction viscosity of polyimide) A polyimide solution was prepared by dissolving polyimide powder in N,N-dimethylacetamide (DMAC) so as to have a concentration of 0.5 g/dL . Using an Ubbelohde viscometer, the outflow time (T) of the polyimide solution at a temperature of 30° C. and the outflow time (T0) of the DMAC alone as the solvent were measured, and the reduced viscosity was obtained by the following formula. Reduced viscosity (dL/g)=(T-T0)/T0/0.5

(聚醯亞胺之重量平均分子量的測定方法)   準備1mg/mL的濃度之聚醯亞胺的四氫呋喃溶液,使用尺寸排除層析裝置(東曹股份有限公司製HLC-8320GPC),以溶離液:四氫呋喃(不含安定劑)、管柱:TSKgel SuperHM-M(2管直列)、檢出器:示差折射計、測定溫度:40℃、流量:0.6mL/min、注入量:40μL的條件測定。分子量為藉由標準物質換算的相對分子量值算出(標準物質:標準聚苯乙烯12點(分子量504~1,090,000)、檢量線:3次近似曲線)。(Measurement method of weight average molecular weight of polyimide) Prepare a tetrahydrofuran solution of polyimide with a concentration of 1 mg/mL, and use a size exclusion chromatography apparatus (HLC-8320GPC manufactured by Tosoh Corporation) to elute: Measured under the conditions of tetrahydrofuran (stabilizer-free), column: TSKgel SuperHM-M (two tubes in-line), detector: differential refractometer, measurement temperature: 40°C, flow rate: 0.6 mL/min, injection volume: 40 μL. The molecular weight was calculated as a relative molecular weight value converted from a standard substance (standard substance: standard polystyrene 12 points (molecular weight 504 to 1,090,000), calibration curve: a cubic approximation curve).

(聚醯亞胺粉體之平均粒徑的測定方法)   使用雷射繞射/散射式粒徑分布測定裝置(堀場製作所股份有限公司製LA-950V2),使用乙醇作為分散媒來測定。(Measuring Method of Average Particle Size of Polyimide Powder) Using a laser diffraction/scattering particle size distribution analyzer (LA-950V2 manufactured by Horiba Seisakusho Co., Ltd.), it was measured using ethanol as a dispersing medium.

(聚醯亞胺之全光線透過率及黃色度的測定方法) (1)測定用薄膜樣品之作成方法   將聚醯亞胺粉體以成為於下述實施例或比較例所指定的量的方式溶解在N,N-二甲基乙醯胺。接著使用施用器,於平滑之玻璃板上以乾燥後厚度成為50μm的方式進行製膜,於熱風烤箱內以130℃保持60分鐘後,於從130℃至260℃為止以5℃/分鐘進行昇溫,進而於260℃保持10分鐘進行乾燥,然後從熱風烤箱取出,冷卻至室溫後,從玻璃板剝離作為測定用之聚醯亞胺薄膜樣品。(Measuring method of total light transmittance and yellowness of polyimide) (1) Preparation method of film sample for measurement Polyimide powder was made into the amount specified in the following Examples or Comparative Examples. Dissolved in N,N-dimethylacetamide. Next, using an applicator, a film was formed on a smooth glass plate so as to have a thickness of 50 μm after drying, and the temperature was increased at 5°C/min from 130°C to 260°C after holding it in a hot air oven at 130°C for 60 minutes. , and further dried at 260° C. for 10 minutes, then taken out from the hot air oven, cooled to room temperature, and peeled off from the glass plate as a polyimide film sample for measurement.

(2)全光線透過率的測定   使用分光色彩計(柯尼卡美能達股份有限公司製、CM-5),根據ASTM E 1164,以光源C、視角2°的條件,求出薄膜厚度50μm時之全光線透過率。(2) Measurement of total light transmittance Using a spectrocolorimeter (manufactured by Konica Minolta Co., Ltd., CM-5), according to ASTM E 1164, under the conditions of light source C and viewing angle of 2°, when the film thickness is 50 μm the total light transmittance.

(3)黃色度(YI)的測定   使用分光色彩計(柯尼卡美能達股份有限公司製、CM-5),根據ASTM D 1925,以光源C、視角2°的條件,於360~740nm的波長範圍進行掃描,求出薄膜厚度50μm時之黃色度(YI)。(3) Measurement of yellowness (YI) Using a spectrocolorimeter (manufactured by Konica Minolta Co., Ltd., CM-5), according to ASTM D 1925, under the conditions of light source C and viewing angle of 2°, at 360 to 740 nm The wavelength range was scanned, and the yellowness (YI) at a film thickness of 50 μm was obtained.

(聚醯亞胺薄膜之拉伸強度及伸長度的測定方法)   藉由與聚醯亞胺之全光線透過率及黃色度的測定所使用之聚醯亞胺薄膜的製造方法相同的方法,以於聚醯亞胺薄膜不會進入異物或氣泡等之缺點的方式注意,作成聚醯亞胺薄膜。其次將所得之聚醯亞胺薄膜使用羽毛刀片切成10mm×150mm之尺寸,作成10條之試驗片。將所得之試驗片使用拉伸試驗機(島津製作所股份有限公司製 Autograph AGS-X load cell 500N),以夾頭間距離50mm、拉伸速度50mm/分鐘的速度進行拉伸試驗,測定破斷時之拉伸強度與伸長度,將10次之試驗的平均值作為個別的拉伸強度與伸長度求出。(Measuring method of tensile strength and elongation of polyimide film) By the same method as the manufacturing method of the polyimide film used in the measurement of the total light transmittance and yellowness of polyimide, to The polyimide film was prepared in such a way that the polyimide film did not have the disadvantage that foreign matter, air bubbles, etc. would not enter. Next, the obtained polyimide film was cut into a size of 10 mm×150 mm using a feather blade, and 10 test pieces were prepared. The obtained test piece was subjected to a tensile test using a tensile tester (Autograph AGS-X load cell 500N manufactured by Shimadzu Corporation) at a distance between the chucks of 50 mm and a tensile speed of 50 mm/min, and the time of breaking was measured. For the tensile strength and elongation, the average value of 10 tests was obtained as the individual tensile strength and elongation.

(實施例X1)   於具備攪拌裝置與攪拌葉片之玻璃製之2L的可分離燒瓶,放入溶劑N,N-二甲基乙醯胺(DMAC)461g(含有100ppm之水分。以下,於全部之實施例X與比較例X使用之DMAC亦相同)與具有氟基之芳香族二胺化合物即2,2’-雙(三氟甲基)-4,4’-二胺基聯苯基(TFMB)64.047g(0.2000莫耳)進行攪拌,使TFMB溶解在DMAC中。其次,邊攪拌可分離燒瓶內,邊於氮氣流下,將四羧酸二酐之4,4’-(1,1,1,3,3,3-六氟丙烷-2,2-二基)二鄰苯二甲酸二酐(6FDA)89.737g(0.2020莫耳)分成10分鐘左右投入,邊直接以溫度成為20~40℃的溫度範圍的方式進行調整邊持續攪拌6小時,來進行聚合反應,而得到黏稠之聚醯胺酸溶液。使用之四羧酸二酐/芳香族二胺化合物的莫耳比率為1.01,聚醯胺酸溶液的濃度為25重量%。(Example X1) 461 g of solvent N,N-dimethylacetamide (DMAC) (containing 100 ppm of water. Hereinafter, in all Example X and Comparative Example X used the same DMAC) and 2,2'-bis(trifluoromethyl)-4,4'-diaminobiphenyl (TFMB), an aromatic diamine compound having a fluorine group. ) 64.047 g (0.2000 moles) were stirred to dissolve TFMB in DMAC. Next, while stirring the inside of the separable flask, under nitrogen flow, tetracarboxylic dianhydride 4,4'-(1,1,1,3,3,3-hexafluoropropane-2,2-diyl) Diphthalic acid dianhydride (6FDA) 89.737 g (0.2020 mol) was divided into about 10 minutes, and the polymerization reaction was carried out while continuously stirring for 6 hours while adjusting the temperature so that the temperature was in the temperature range of 20 to 40°C. A viscous polyamide solution was obtained. The molar ratio of the used tetracarboxylic dianhydride/aromatic diamine compound was 1.01, and the concentration of the polyamic acid solution was 25% by weight.

於所得之聚醯胺酸溶液加入DMAC410g,以聚醯胺酸的濃度成為15重量%的方式進行稀釋後,加入異喹啉25.83g作為醯亞胺化促進劑,邊攪拌聚醯胺酸溶液邊保持在30~40℃的溫度範圍,作為醯亞胺化劑,係對其邊耗費約10分鐘緩緩滴下乙酸酐122.5g(1.20莫耳)邊投入,然後進而將液溫保持在30~40℃持續攪拌12小時,進行化學醯亞胺化反應,而得到聚醯亞胺溶液。410 g of DMAC was added to the obtained polyamic acid solution, and after diluting so that the concentration of polyamic acid became 15% by weight, 25.83 g of isoquinoline was added as an imidization accelerator, and the polyamic acid solution was stirred while stirring. Maintained at a temperature range of 30 to 40°C, as an imidizing agent, 122.5 g (1.20 mol) of acetic anhydride was slowly added dropwise to it for about 10 minutes, and then the liquid temperature was maintained at 30 to 40 °C. The stirring was continued at °C for 12 hours, and the chemical imidization reaction was carried out to obtain a polyimide solution.

接著,將包含所得之醯亞胺化劑及醯亞胺化促進劑的聚醯亞胺溶液1000g,轉移至具備攪拌裝置與攪拌葉片之5L的可分離燒瓶,邊以120rpm的速度攪拌邊保持在15~25℃的溫度,對其將甲醇1500g以10g/分鐘的速度滴下。投入約800g之甲醇時,確認聚醯亞胺溶液的濁度,確認粉體狀之聚醯亞胺的析出。接著投入1500g全量之甲醇,完成聚醯亞胺的析出。Next, 1,000 g of a polyimide solution containing the obtained imidization agent and imidization accelerator was transferred to a 5-L separable flask equipped with a stirring device and a stirring blade, and kept at 120 rpm while being stirred at a speed of 120 rpm. At a temperature of 15 to 25°C, 1500 g of methanol was dropped thereon at a rate of 10 g/min. When about 800 g of methanol was put in, the turbidity of the polyimide solution was confirmed, and the precipitation of powdery polyimide was confirmed. Next, 1500 g of methanol in total was put in to complete the precipitation of polyimide.

其次,將可分離燒瓶的內容物藉由吸引過濾裝置濾除,進而使用1000g之甲醇進行洗淨暨濾除。Next, the contents of the separable flask were filtered off by a suction filtration device, and further washed and filtered using 1000 g of methanol.

然後,將經濾除之聚醯亞胺粉體50g使用附有局部排氣裝置之乾燥機,於50℃乾燥24小時,進而於260℃乾燥2小時,去除殘留之揮發成分,而得到聚醯亞胺粉體(a-1)。對於聚醯亞胺粉體(a-1)所測定之還原黏度為1.52dL/g。Then, 50 g of the filtered polyimide powder was dried at 50° C. for 24 hours using a dryer equipped with a local exhaust device, and further dried at 260° C. for 2 hours to remove residual volatile components to obtain polyimide. Imine powder (a-1). The reduced viscosity measured for the polyimide powder (a-1) was 1.52 dL/g.

接著,與聚醯亞胺粉體(a-1)相同,將DMAC460g與TFMB64.047g(0.200莫耳)放入2L的可分離燒瓶進行攪拌,使TFMB溶解在DMAC中。其次,邊攪拌可分離燒瓶內邊於氮氣流下,耗費10分鐘左右投入6FDA89.204g(0.2008莫耳),邊直接以溫度成為20~40℃的溫度範圍的方式進行調整邊持續攪拌6小時,來進行聚合反應,而得到黏稠之聚醯胺酸溶液。使用之四羧酸二酐/芳香族二胺化合物的莫耳比率為1.004,聚醯胺酸溶液的濃度為25重量%。Next, similarly to the polyimide powder (a-1), 460 g of DMAC and 64.047 g (0.200 mol) of TFMB were put into a 2 L separable flask and stirred to dissolve TFMB in DMAC. Next, 6FDA89.204 g (0.2008 mol) was poured into the separable flask while stirring the inside of the separable flask under nitrogen flow for about 10 minutes, and the stirring was continued for 6 hours while adjusting the temperature to be in the temperature range of 20 to 40°C. A polymerization reaction was carried out to obtain a viscous polyamide solution. The molar ratio of the used tetracarboxylic dianhydride/aromatic diamine compound was 1.004, and the concentration of the polyamic acid solution was 25% by weight.

之後與聚醯亞胺粉體(a-1)相同進行化學醯亞胺化、粉體化、乾燥,而得到由還原黏度為2.54dL/g之聚醯亞胺所構成之聚醯亞胺粉體(b-1)。Then, chemical imidization, powderization, and drying were carried out in the same manner as the polyimide powder (a-1) to obtain a polyimide powder composed of polyimide having a reduced viscosity of 2.54 dL/g. body (b-1).

將所得之聚醯亞胺粉體(a-1)20g與聚醯亞胺粉體(b-1)20g,置入回轉型之混合裝置耗費1小時以上充分混合,而得到作為目的之聚醯亞胺粉體。對於所得之聚醯亞胺粉體所測定之還原黏度為2.03dL/g,平均粒徑為0.06mm。20 g of the obtained polyimide powder (a-1) and 20 g of the polyimide powder (b-1) were placed in a rotary mixer for more than 1 hour and fully mixed to obtain the intended polyimide imine powder. The reduced viscosity measured for the obtained polyimide powder was 2.03 dL/g, and the average particle size was 0.06 mm.

其次,混合聚醯亞胺粉體(a-1)與聚醯亞胺粉體(b-1),將所得之聚醯亞胺粉體20g溶解在80g之DMAC成為均一之聚醯亞胺溶液後,使用施用器,塗膜於玻璃板上,以指定的條件使DMAC乾燥後,從玻璃板剝離作成50μm厚度的聚醯亞胺薄膜。所得之聚醯亞胺薄膜的全光線透過率高至90%,黃色度為1.3,即使目視亦未觀察到變色,係透明性極為優異者。又,聚醯亞胺薄膜之拉伸試驗的結果,係拉伸強度160MPa、伸長度70%之優異者。Next, mix the polyimide powder (a-1) and the polyimide powder (b-1), and dissolve 20 g of the obtained polyimide powder in 80 g of DMAC to obtain a uniform polyimide solution Then, using an applicator, a film was applied to a glass plate, and DMAC was dried under predetermined conditions, and then peeled off from the glass plate to prepare a polyimide film having a thickness of 50 μm. The total light transmittance of the obtained polyimide film was as high as 90%, the yellowness was 1.3, the discoloration was not observed even by visual observation, and the transparency was extremely excellent. In addition, as a result of the tensile test of the polyimide film, it was excellent in a tensile strength of 160 MPa and an elongation of 70%.

(實施例X2)   除了使用由於實施例X1所得之還原黏度為1.52dL/g之聚醯亞胺所構成之聚醯亞胺粉體(a-1)16g,使用由還原黏度為2.54dL/g之聚醯亞胺所構成之聚醯亞胺粉體(b-1)24g,將聚醯亞胺粉體(a-1)與聚醯亞胺粉體(b-1)的混合比率,以重量比率成為聚醯亞胺粉體(a-1)/聚醯亞胺粉體(b-1)=40/60之外,其他與實施例X1同樣進行。(Example X2) In addition to using 16 g of polyimide powder (a-1) composed of polyimide having a reduced viscosity of 1.52 dL/g obtained in Example X1, the reduced viscosity of 2.54 dL/g was used. 24 g of polyimide powder (b-1) composed of The weight ratio was carried out in the same manner as in Example X1 except that the polyimide powder (a-1)/polyimide powder (b-1)=40/60.

對於所得之聚醯亞胺粉體所測定之還原黏度為2.13dL/g,平均粒徑為0.06mm。又,由此聚醯亞胺粉體所得之50μm厚度的聚醯亞胺薄膜的全光線透過率高至90%,黃色度為1.3,係透明性極為優異者。又,聚醯亞胺薄膜的拉伸強度為165MPa。伸長度72%為優異者。The reduced viscosity measured for the obtained polyimide powder was 2.13 dL/g, and the average particle size was 0.06 mm. Moreover, the total light transmittance of the 50-μm-thick polyimide film obtained from the polyimide powder was as high as 90%, the yellowness was 1.3, and the transparency was extremely excellent. In addition, the tensile strength of the polyimide film was 165 MPa. An elongation of 72% was considered excellent.

(實施例X3)   除了使用由於實施例X1所得之還原黏度為1.52dL/g之聚醯亞胺所構成之聚醯亞胺粉體(a-1)14g,使用由還原黏度為2.54dL/g之聚醯亞胺所構成之聚醯亞胺粉體(b-1)26g,將聚醯亞胺粉體(a-1)與聚醯亞胺粉體(b-1)的混合比率,以重量比率成為聚醯亞胺粉體(a-1)/聚醯亞胺粉體(b-1)=35/65之外,其他與實施例X1同樣進行。(Example X3) In addition to using 14 g of polyimide powder (a-1) composed of polyimide having a reduced viscosity of 1.52 dL/g obtained in Example X1, a reduced viscosity of 2.54 dL/g was used. 26g of polyimide powder (b-1) composed of The weight ratio was carried out in the same manner as in Example X1 except that the weight ratio was polyimide powder (a-1)/polyimide powder (b-1)=35/65.

對於所得之聚醯亞胺粉體所測定之還原黏度為2.18dL/g,平均粒徑為0.06mm。又,由此聚醯亞胺粉體所得之50μm厚度的聚醯亞胺薄膜的全光線透過率高至91%,黃色度為1.3,係透明性極為優異者。又,聚醯亞胺薄膜的拉伸強度為160MPa。伸長度70%為優異者。The reduced viscosity measured for the obtained polyimide powder was 2.18 dL/g, and the average particle size was 0.06 mm. Moreover, the total light transmittance of the 50-μm-thick polyimide film obtained from the polyimide powder was as high as 91%, the yellowness was 1.3, and the transparency was extremely excellent. In addition, the tensile strength of the polyimide film was 160 MPa. An elongation of 70% was considered excellent.

(實施例X4)   除了將聚醯亞胺粉體(a-1)的合成所使用之6FDA的使用量並非定為89.737g(0.2020莫耳),而是定為89.559g(0.2016莫耳),將四羧酸二酐/芳香族二胺化合物的莫耳比率定為1.008之外,其他與實施例X1相同進行聚醯亞胺粉體(a-1)的合成,而得到由還原黏度為1.83dL/g之聚醯亞胺所構成之聚醯亞胺粉體(a-1)。(Example X4) Except that the usage amount of 6FDA used in the synthesis of the polyimide powder (a-1) was not 89.737g (0.2020 mol), but 89.559 g (0.2016 mol), The polyimide powder (a-1) was synthesized in the same manner as in Example X1 except that the molar ratio of the tetracarboxylic dianhydride/aromatic diamine compound was set to 1.008, and the reduced viscosity was 1.83. Polyimide powder (a-1) composed of dL/g of polyimide.

其次,將所得之還原黏度1.83dL/g的聚醯亞胺粉體(a-1)30g與於實施例X1所得之還原黏度2.54dL/g的聚醯亞胺粉體(b-1)10g,置入回轉型之混合裝置耗費1小時以上充分混合,而得到聚醯亞胺粉體(a-1)/聚醯亞胺粉體(b-1)的重量比率為75/25之聚醯亞胺粉體。Next, 30 g of the obtained polyimide powder (a-1) with a reduced viscosity of 1.83 dL/g and 10 g of the polyimide powder (b-1) with a reduced viscosity of 2.54 dL/g obtained in Example X1 , it takes more than 1 hour to fully mix in the mixing device of the rotary type, and the weight ratio of polyimide powder (a-1)/polyimide powder (b-1) is 75/25. imine powder.

對於所得之聚醯亞胺粉體所測定之還原黏度為2.01dL/g,平均粒徑為0.08mm。The reduced viscosity measured for the obtained polyimide powder was 2.01 dL/g, and the average particle size was 0.08 mm.

以下,與實施例X1同樣進行所作成之50μm厚度的聚醯亞胺薄膜的全光線透過率高至91%,黃色度為1.3,即使目視亦未觀察到變色,係透明性極為優異者。又,聚醯亞胺薄膜的拉伸強度為155MPa,伸長度為65%。Hereinafter, the polyimide film with a thickness of 50 μm produced in the same manner as in Example X1 had a high total light transmittance of 91%, a yellowness of 1.3, no discoloration was observed even by visual observation, and it was extremely excellent in transparency. In addition, the tensile strength of the polyimide film was 155 MPa, and the elongation was 65%.

(實施例X5)   除了將聚醯亞胺粉體(b-1)的合成所使用之6FDA的使用量並非定為89.204g(0.2008莫耳),而是定為89.293g(0.2010莫耳),將四羧酸二酐/芳香族二胺化合物的莫耳比率定為1.005之外,其他與實施例X1相同進行聚醯亞胺粉體(b-1)的合成,而得到由還原黏度為2.26dL/g之聚醯亞胺所構成之聚醯亞胺粉體(b-1)。(Example X5) Except that the usage amount of 6FDA used in the synthesis of the polyimide powder (b-1) was not 89.204g (0.2008 mol), but 89.293 g (0.2010 mol), The polyimide powder (b-1) was synthesized in the same manner as in Example X1 except that the molar ratio of the tetracarboxylic dianhydride/aromatic diamine compound was set to 1.005, and the reduced viscosity was 2.26. Polyimide powder (b-1) composed of dL/g polyimide.

其次,將實施例X1所得之還原黏度1.52dL/g的聚醯亞胺粉體(a-1)10g與本實施例之還原黏度2.26dL/g的聚醯亞胺粉體(b-1)30g,置入回轉型之混合裝置耗費1小時以上充分混合,而得到聚醯亞胺粉體(a-1)/聚醯亞胺粉體(b-1)的重量比率為25/75之聚醯亞胺粉體。Next, 10 g of the polyimide powder (a-1) with a reduced viscosity of 1.52 dL/g obtained in Example X1 and the polyimide powder (b-1) with a reduced viscosity of 2.26 dL/g obtained in this example were combined. 30g, put it into the mixing device of the rotary type and spend more than 1 hour to mix thoroughly to obtain a polyimide powder (a-1)/polyimide powder (b-1) with a weight ratio of 25/75. Imide powder.

對於所得之聚醯亞胺粉體所測定之還原黏度為2.08dL/g,平均粒徑為0.09mm。The reduced viscosity measured for the obtained polyimide powder was 2.08 dL/g, and the average particle size was 0.09 mm.

以下,與實施例X1同樣進行所作成之50μm厚度的聚醯亞胺薄膜的全光線透過率高至90%,黃色度為1.3,即使目視亦未觀察到變色,係透明性極為優異者。又,聚醯亞胺薄膜的拉伸強度為158MPa,伸長度為68%。Hereinafter, the polyimide film with a thickness of 50 μm produced in the same manner as in Example X1 had a high total light transmittance of 90%, a yellowness of 1.3, and no discoloration was observed even by visual inspection, which was extremely excellent in transparency. In addition, the tensile strength of the polyimide film was 158 MPa, and the elongation was 68%.

(實施例X6)   除了將聚醯亞胺粉體(a-1)的合成所使用之DMAC的使用量並非定為461g而是定為485g,作為芳香族二胺化合物,取代TFMB64.047g(0.2000莫耳),改使用TFMB51.238g (0.1600莫耳)及2,2-雙[4-(4-胺基苯氧基)苯基]-1,1,1,3,3,3-六氟丙烷(BAPP-F)20.738g(0.0400莫耳),進行化學醯亞胺化反應前所使用之稀釋用DMAC的使用量並非定為410g而是定為431g之外,其他與實施例X1相同進行聚醯亞胺粉體(a-1)的合成,作為芳香族二胺化合物,得到TFMB以及BAPP-F,及作為四羧酸二酐,得到由6FDA所合成之還原黏度為1.59dL/g之聚醯亞胺所構成之聚醯亞胺粉體(a-1)。(Example X6) Except that the amount of DMAC used in the synthesis of the polyimide powder (a-1) was not 461 g but 485 g, as the aromatic diamine compound, 64.047 g (0.2000 g (0.2000 g) TFMB was replaced mol), use TFMB51.238g (0.1600 mol) and 2,2-bis[4-(4-aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoro Propane (BAPP-F) 20.738g (0.0400mol), the amount of DMAC used for dilution before the chemical imidization reaction was not set at 410g but set at 431g, the other was carried out in the same way as in Example X1 Synthesis of polyimide powder (a-1), as an aromatic diamine compound, obtains TFMB and BAPP-F, and as a tetracarboxylic dianhydride, obtains a compound with a reduced viscosity of 1.59 dL/g synthesized by 6FDA Polyimide powder (a-1) composed of polyimide.

將所得之還原黏度1.59dL/g的聚醯亞胺粉體(a-1)20g與於實施例X1所得之還原黏度2.54dL/g的聚醯亞胺粉體(b-1)20g,置入回轉型之混合裝置耗費1小時以上充分混合,而得到聚醯亞胺粉體(a-1)/聚醯亞胺粉體(b-1)的重量比率為50/50之聚醯亞胺粉體。20 g of the obtained polyimide powder (a-1) with a reduced viscosity of 1.59 dL/g and 20 g of the polyimide powder (b-1) with a reduced viscosity of 2.54 dL/g obtained in Example X1 were put into It takes more than 1 hour to fully mix in the mixing device of the rotary type, and the weight ratio of the polyimide powder (a-1)/polyimide powder (b-1) is 50/50 to obtain the polyimide powder.

對於所得之聚醯亞胺粉體所測定之還原黏度為2.07dL/g,平均粒徑為0.10mm。The reduced viscosity measured for the obtained polyimide powder was 2.07 dL/g, and the average particle size was 0.10 mm.

以下,與實施例X1同樣進行所作成之50μm厚度的聚醯亞胺薄膜的全光線透過率高至89%,黃色度為1.4,即使目視亦未觀察到變色,係透明性極為優異者。又,聚醯亞胺薄膜的拉伸強度為150MPa,伸長度為60%。Hereinafter, the polyimide film with a thickness of 50 μm produced in the same manner as in Example X1 had a high total light transmittance of 89%, a yellowness of 1.4, and no discoloration was observed even by visual observation, which was extremely excellent in transparency. In addition, the tensile strength of the polyimide film was 150 MPa, and the elongation was 60%.

(實施例X7)   作成聚醯亞胺塗料A與聚醯亞胺塗料B,該聚醯亞胺塗料A係將於實施例X1所得之還原黏度1.52dL/g的聚醯亞胺粉體(a-1)20g溶解在80g之DMAC,該聚醯亞胺塗料B係將於實施例X1所得之還原黏度2.54dL/g的聚醯亞胺粉體(b-1)20g溶解在80g之DMAC,混合聚醯亞胺塗料A50g(溶解溶質之聚醯亞胺粉體(a-1)10g)與聚醯亞胺塗料B50g(溶解溶質之聚醯亞胺粉體(b-1)10g),而得到作為目的之聚醯亞胺塗料。(Example X7) A polyimide coating A and a polyimide coating B were prepared. The polyimide coating A was the polyimide powder with a reduced viscosity of 1.52 dL/g obtained in Example X1 (a -1) 20 g is dissolved in 80 g of DMAC, the polyimide coating B is to dissolve 20 g of the polyimide powder (b-1) with a reduced viscosity of 2.54 dL/g obtained in Example X1 in 80 g of DMAC, Mixing polyimide coating A50g (polyimide powder (a-1) 10g dissolved solute) and polyimide coating B50g (polyimide powder (b-1) 10g dissolved solute), and The intended polyimide paint was obtained.

將所得之聚醯亞胺塗料定為0.5g/dL的濃度所測定之還原黏度為2.03dL/g。The obtained polyimide coating was determined to have a concentration of 0.5 g/dL, and the measured reduced viscosity was 2.03 dL/g.

以下,與實施例X1同樣進行所作成之50μm厚度的聚醯亞胺薄膜的全光線透過率高至90%,黃色度為1.3,即使目視亦未觀察到變色,係透明性極為優異者。又,聚醯亞胺薄膜的拉伸強度為165MPa,伸長度為70%。Hereinafter, the polyimide film with a thickness of 50 μm produced in the same manner as in Example X1 had a high total light transmittance of 90%, a yellowness of 1.3, and no discoloration was observed even by visual inspection, which was extremely excellent in transparency. In addition, the tensile strength of the polyimide film was 165 MPa, and the elongation was 70%.

(比較例X1)   僅將於實施例X1合成之還原黏度1.52dL/g的聚醯亞胺粉體(a-1)20g溶解在80g之DMAC,而成為均一之聚醯亞胺溶液後,使用施用器塗膜在玻璃板上,以指定的條件乾燥DMAC後,從玻璃板剝離作成50μm厚度的聚醯亞胺薄膜時,成為所得之聚醯亞胺薄膜的全光線透過率為89%,黃色度為1.8,拉伸強度為125MPa,伸長度為20%之低的結果。(Comparative Example X1) Only 20 g of the polyimide powder (a-1) with a reduced viscosity of 1.52 dL/g synthesized in Example X1 was dissolved in 80 g of DMAC to obtain a uniform polyimide solution, and then used When the applicator coats the film on the glass plate, after drying DMAC under the specified conditions, the polyimide film with a thickness of 50 μm is peeled off from the glass plate, and the total light transmittance of the obtained polyimide film is 89%, yellow Degree of 1.8, tensile strength of 125MPa, and elongation as low as 20%.

(比較例X2)   僅將於實施例X1合成之還原黏度2.54dL/g的聚醯亞胺粉體(b-1)20g溶解在80g之DMAC時,聚醯亞胺塗料的黏度過高,難以成為適合塗膜之黏度的塗料。因此,進而追加60gDMAC作為12.5%之塗料後,使用施用器塗膜在玻璃板上,以指定的條件乾燥DMAC後,從玻璃板剝離作成50μm厚度的聚醯亞胺薄膜。所得之聚醯亞胺薄膜的全光線透過率雖為90%,黃色度1.3,但拉伸強度為145MPa,伸長度為40%時,與上述實施例X比較,成為較低的結果。(Comparative Example X2) Only when 20 g of the polyimide powder (b-1) with a reduced viscosity of 2.54 dL/g synthesized in Example X1 was dissolved in 80 g of DMAC, the viscosity of the polyimide coating was too high, making it difficult to A paint suitable for the viscosity of the coating film. Therefore, after further adding 60 g of DMAC as a 12.5% coating material, the film was coated on a glass plate using an applicator, and after drying DMAC under the specified conditions, it was peeled off from the glass plate to prepare a polyimide film with a thickness of 50 μm. Although the total light transmittance of the obtained polyimide film was 90% and the yellowness was 1.3, the tensile strength was 145 MPa and the elongation was 40%, which was lower than that of Example X above.

將結果集中在表1。

Figure 02_image001
The results are gathered in Table 1.
Figure 02_image001

(實施例Y1)   於具備攪拌裝置與攪拌葉片之玻璃製之2L的可分離燒瓶,放入溶劑N,N-二甲基乙醯胺(DMAC)461g(含有100ppm之水分。以下,於全部之實施例Y與比較例Y使用之DMAC亦相同)與具有氟基之芳香族二胺化合物即2,2’-雙(三氟甲基)-4,4’-二胺基聯苯基(TFMB)64.047g(0.2000莫耳)進行攪拌,使TFMB溶解在DMAC中。其次,邊攪拌可分離燒瓶內,邊於氮氣流下,將四羧酸二酐之4,4’-(1,1,1,3,3,3-六氟丙烷-2,2-二基)二鄰苯二甲酸二酐(6FDA)89.737g(0.2020莫耳)分成10分鐘左右投入,邊直接以溫度成為20~40℃的溫度範圍的方式進行調整邊持續攪拌6小時,來進行聚合反應,而得到黏稠之聚醯胺酸溶液。使用之四羧酸二酐/芳香族二胺化合物的莫耳比率為1.01,聚醯胺酸溶液的濃度為25重量%。(Example Y1) Into a 2L separable flask made of glass equipped with a stirring device and a stirring blade, put 461 g of solvent N,N-dimethylacetamide (DMAC) (containing 100 ppm of water. Hereinafter, in all Example Y and Comparative Example Y used the same DMAC) and 2,2'-bis(trifluoromethyl)-4,4'-diaminobiphenyl (TFMB), an aromatic diamine compound having a fluorine group. ) 64.047 g (0.2000 moles) were stirred to dissolve TFMB in DMAC. Next, while stirring the inside of the separable flask, under nitrogen flow, tetracarboxylic dianhydride 4,4'-(1,1,1,3,3,3-hexafluoropropane-2,2-diyl) Diphthalic acid dianhydride (6FDA) 89.737 g (0.2020 mol) was divided into about 10 minutes, and the polymerization reaction was carried out while continuously stirring for 6 hours while adjusting the temperature so that the temperature was in the temperature range of 20 to 40°C. A viscous polyamide solution was obtained. The molar ratio of the used tetracarboxylic dianhydride/aromatic diamine compound was 1.01, and the concentration of the polyamic acid solution was 25% by weight.

於所得之聚醯胺酸溶液加入DMAC410g,以聚醯胺酸的濃度成為15重量%的方式進行稀釋後,加入異喹啉25.83g作為醯亞胺化促進劑,邊攪拌聚醯胺酸溶液邊保持在30~40℃的溫度範圍,作為醯亞胺化劑,係邊對其耗費約10分鐘緩緩滴下乙酸酐122.5g(1.20莫耳)邊投入,然後進而將液溫保持在30~40℃持續攪拌12小時,進行化學醯亞胺化反應,而得到聚醯亞胺溶液。410 g of DMAC was added to the obtained polyamic acid solution, and after diluting so that the concentration of polyamic acid became 15% by weight, 25.83 g of isoquinoline was added as an imidization accelerator, and the polyamic acid solution was stirred while stirring. It was kept in a temperature range of 30 to 40°C, and as an imidizing agent, 122.5 g (1.20 mol) of acetic anhydride was slowly added dropwise to it for about 10 minutes, and then the liquid temperature was kept at 30 to 40 The stirring was continued at °C for 12 hours, and the chemical imidization reaction was carried out to obtain a polyimide solution.

接著,將包含所得之醯亞胺化劑及醯亞胺化促進劑的聚醯亞胺溶液1000g,轉移至具備攪拌裝置與攪拌葉片之5L的可分離燒瓶,邊以120rpm的速度攪拌邊保持在15~25℃的溫度,對其將甲醇1500g以10g/分鐘的速度滴下。投入約800g之甲醇時,確認聚醯亞胺溶液的濁度,確認粉體狀之聚醯亞胺的析出。接著投入1500g全量之甲醇,完成聚醯亞胺的析出。Next, 1,000 g of a polyimide solution containing the obtained imidization agent and imidization accelerator was transferred to a 5-L separable flask equipped with a stirring device and a stirring blade, and kept at 120 rpm while being stirred at a speed of 120 rpm. At a temperature of 15 to 25°C, 1500 g of methanol was dropped thereon at a rate of 10 g/min. When about 800 g of methanol was put in, the turbidity of the polyimide solution was confirmed, and the precipitation of powdery polyimide was confirmed. Next, 1500 g of methanol in total was put in to complete the precipitation of polyimide.

其次,將可分離燒瓶的內容物藉由吸引過濾裝置濾除,進而使用1000g之甲醇進行洗淨暨濾除。Next, the contents of the separable flask were filtered off by a suction filtration device, and further washed and filtered using 1000 g of methanol.

然後,將經濾除之聚醯亞胺粉體50g使用附有局部排氣裝置之乾燥機,於50℃乾燥24小時,進而於260℃乾燥2小時,去除殘留之揮發成分,而得到聚醯亞胺粉體(a-2)。對於聚醯亞胺粉體(a-2)所測定之重量平均分子量為195,000g/mol。Then, 50 g of the filtered polyimide powder was dried at 50° C. for 24 hours using a dryer equipped with a local exhaust device, and further dried at 260° C. for 2 hours to remove residual volatile components to obtain polyimide. Imine powder (a-2). The weight average molecular weight measured for the polyimide powder (a-2) was 195,000 g/mol.

接著,與聚醯亞胺粉體(a-2)相同,將DMAC460g與TFMB64.047g(0.200莫耳)放入2L的可分離燒瓶進行攪拌,使TFMB溶解在DMAC中。其次,邊攪拌可分離燒瓶內邊於氮氣流下,耗費10分鐘左右投入6FDA89.204g(0.2008莫耳),邊直接以溫度成為20~40℃的溫度範圍的方式進行調整邊持續攪拌6小時,來進行聚合反應,而得到黏稠之聚醯胺酸溶液。使用之四羧酸二酐/芳香族二胺化合物的莫耳比率為1.004,聚醯胺酸溶液的濃度為25重量%。Next, similarly to the polyimide powder (a-2), 460 g of DMAC and 64.047 g (0.200 mol) of TFMB were put into a 2 L separable flask and stirred to dissolve TFMB in DMAC. Next, 6FDA89.204 g (0.2008 mol) was poured into the separable flask while stirring the inside of the separable flask under nitrogen flow for about 10 minutes, and the stirring was continued for 6 hours while adjusting the temperature to be in the temperature range of 20 to 40°C. A polymerization reaction was carried out to obtain a viscous polyamide solution. The molar ratio of the used tetracarboxylic dianhydride/aromatic diamine compound was 1.004, and the concentration of the polyamic acid solution was 25% by weight.

之後與聚醯亞胺粉體(a-2)相同進行化學醯亞胺化、粉體化、乾燥,而得到由重量平均分子量為342,000g/mol之聚醯亞胺所構成之聚醯亞胺粉體(b-2)。Then, chemical imidization, powderization, and drying were carried out in the same manner as the polyimide powder (a-2) to obtain a polyimide composed of polyimide having a weight average molecular weight of 342,000 g/mol. Powder (b-2).

將所得之聚醯亞胺粉體(a-2)20g與聚醯亞胺粉體(b-2)20g,置入回轉型之混合裝置耗費1小時以上充分混合,而得到作為目的之聚醯亞胺粉體。對於所得之聚醯亞胺粉體所測定之重量平均分子量為259,000g/mol,平均粒徑為0.06mm。20 g of the obtained polyimide powder (a-2) and 20 g of the polyimide powder (b-2) were placed in a rotary mixer for more than 1 hour and fully mixed to obtain the intended polyimide imine powder. The weight average molecular weight measured for the obtained polyimide powder was 259,000 g/mol, and the average particle diameter was 0.06 mm.

其次,混合聚醯亞胺粉體(a-2)與聚醯亞胺粉體(b-2),將所得之聚醯亞胺粉體20g溶解在80g之DMAC成為均一之聚醯亞胺溶液後,使用施用器,塗膜於玻璃板上,以指定的條件使DMAC乾燥後,從玻璃板剝離作成50μm厚度的聚醯亞胺薄膜。所得之聚醯亞胺薄膜的全光線透過率高至90%,黃色度為1.3,即使目視亦未觀察到變色,係透明性極為優異者。又,聚醯亞胺薄膜之拉伸試驗的結果,係拉伸強度為160MPa,伸長度為70%之優異者。Next, mix the polyimide powder (a-2) and the polyimide powder (b-2), and dissolve 20 g of the obtained polyimide powder in 80 g of DMAC to obtain a uniform polyimide solution Then, using an applicator, a film was applied to a glass plate, and DMAC was dried under predetermined conditions, and then peeled off from the glass plate to prepare a polyimide film having a thickness of 50 μm. The total light transmittance of the obtained polyimide film was as high as 90%, the yellowness was 1.3, the discoloration was not observed even by visual observation, and the transparency was extremely excellent. In addition, as a result of the tensile test of the polyimide film, a tensile strength of 160 MPa and an elongation of 70% were excellent.

(實施例Y2)   除了使用由於實施例Y1所得之重量平均分子量為195,000g/mol之聚醯亞胺所構成之聚醯亞胺粉體(a-2)16g,使用由重量平均分子量為342,000g/mol之聚醯亞胺所構成之聚醯亞胺粉體(b-2)24g,將聚醯亞胺粉體(a-2)與聚醯亞胺粉體(b-2)的混合比率,以重量比率成為聚醯亞胺粉體(a-2)/聚醯亞胺粉體(b-2)=40/60之外,其他與實施例Y1同樣進行。(Example Y2) In addition to using 16 g of polyimide powder (a-2) composed of polyimide having a weight-average molecular weight of 195,000 g/mol obtained in Example Y1, a weight-average molecular weight of 342,000 g was used. 24 g of polyimide powder (b-2) composed of polyimide/mol, the mixing ratio of polyimide powder (a-2) and polyimide powder (b-2) , except that the weight ratio became polyimide powder (a-2)/polyimide powder (b-2)=40/60, the same procedure as in Example Y1 was carried out.

對於所得之聚醯亞胺粉體所測定之重量平均分子量為269,000g/mol,平均粒徑為0.06mm。又,由此聚醯亞胺粉體所得之50μm厚度的聚醯亞胺薄膜的全光線透過率高至90%,黃色度為1.3,係透明性極為優異者。又,聚醯亞胺薄膜的拉伸強度為165MPa。伸長度為72%之優異者。The weight average molecular weight measured for the obtained polyimide powder was 269,000 g/mol, and the average particle diameter was 0.06 mm. Moreover, the total light transmittance of the 50-μm-thick polyimide film obtained from the polyimide powder was as high as 90%, the yellowness was 1.3, and the transparency was extremely excellent. In addition, the tensile strength of the polyimide film was 165 MPa. Excellent elongation of 72%.

(實施例Y3)   除了使用由於實施例Y1所得之重量平均分子量為195,000g/mol之聚醯亞胺所構成之聚醯亞胺粉體(a-2)14g,使用由重量平均分子量為342,000g/mol之聚醯亞胺所構成之聚醯亞胺粉體(b-2)26g,將聚醯亞胺粉體(a-2)與聚醯亞胺粉體(b-2)的混合比率,以重量比率成為聚醯亞胺粉體(a-2)/聚醯亞胺粉體(b-2)=35/65之外,其他與實施例Y1同樣進行。(Example Y3) In addition to using 14 g of the polyimide powder (a-2) composed of the polyimide having a weight average molecular weight of 195,000 g/mol obtained in Example Y1, a weight average molecular weight of 342,000 g was used. 26 g of polyimide powder (b-2) composed of polyimide/mol, the mixing ratio of polyimide powder (a-2) and polyimide powder (b-2) , except that the weight ratio is polyimide powder (a-2)/polyimide powder (b-2)=35/65, the same procedure as in Example Y1 was carried out.

對於所得之聚醯亞胺粉體所測定之重量平均分子量為280,000g/mol,平均粒徑為0.06mm。又,由此聚醯亞胺粉體所得之50μm厚度的聚醯亞胺薄膜的全光線透過率高至91%,黃色度為1.3,係透明性極為優異者。又,聚醯亞胺薄膜的拉伸強度為160MPa。伸長度為70%之優異者。The weight average molecular weight measured for the obtained polyimide powder was 280,000 g/mol, and the average particle diameter was 0.06 mm. Moreover, the total light transmittance of the 50-μm-thick polyimide film obtained from the polyimide powder was as high as 91%, the yellowness was 1.3, and the transparency was extremely excellent. In addition, the tensile strength of the polyimide film was 160 MPa. The elongation is excellent at 70%.

(實施例Y4)   除了將聚醯亞胺粉體(a-2)的合成所使用之6FDA的使用量並非定為89.737g(0.2020莫耳),而是定為89.559g(0.2016莫耳),將四羧酸二酐/芳香族二胺化合物的莫耳比率定為1.008之外,其他與實施例Y1相同進行聚醯亞胺粉體(a-2)的合成,而得到由重量平均分子量為210,000g/mol之聚醯亞胺所構成之聚醯亞胺粉體(a-2)。(Example Y4) Except that the usage amount of 6FDA used in the synthesis of the polyimide powder (a-2) is not 89.737g (0.2020 mol), but 89.559 g (0.2016 mol), The polyimide powder (a-2) was synthesized in the same manner as in Example Y1, except that the molar ratio of the tetracarboxylic dianhydride/aromatic diamine compound was set to 1.008, and the weight average molecular weight was Polyimide powder (a-2) composed of 210,000 g/mol of polyimide.

其次,將所得之重量平均分子量210,000 g/mol的聚醯亞胺粉體(a-2)30g與於實施例Y1所得之重量平均分子量342,000g/mol的聚醯亞胺粉體(b-2)10g,置入回轉型之混合裝置耗費1小時以上充分混合,而得到聚醯亞胺粉體(a-2)/聚醯亞胺粉體(b-2)的重量比率為75/25之聚醯亞胺粉體。Next, 30 g of the obtained polyimide powder (a-2) with a weight average molecular weight of 210,000 g/mol and the polyimide powder (b-2) with a weight average molecular weight of 342,000 g/mol obtained in Example Y1 were combined. ) 10g, put it into the mixing device of the rotary type and spend more than 1 hour to mix thoroughly, and the weight ratio of the obtained polyimide powder (a-2)/polyimide powder (b-2) is 75/25. Polyimide powder.

對於所得之聚醯亞胺粉體所測定之重量平均分子量為255,000g/mol,平均粒徑為0.08mm。The weight average molecular weight measured for the obtained polyimide powder was 255,000 g/mol, and the average particle diameter was 0.08 mm.

以下,與實施例X1同樣進行所作成之50μm厚度的聚醯亞胺薄膜的全光線透過率高至91%,黃色度為1.3,即使目視亦未觀察到變色,係透明性極為優異者。又,聚醯亞胺薄膜的拉伸強度為155MPa,伸長度為65%。Hereinafter, the polyimide film with a thickness of 50 μm produced in the same manner as in Example X1 had a high total light transmittance of 91%, a yellowness of 1.3, no discoloration was observed even by visual observation, and it was extremely excellent in transparency. In addition, the tensile strength of the polyimide film was 155 MPa, and the elongation was 65%.

(實施例Y5)   除了將聚醯亞胺粉體(b-2)的合成所使用之6FDA的使用量並非定為89.204g(0.2008莫耳),而是定為89.293g(0.2010莫耳),將四羧酸二酐/芳香族二胺化合物的莫耳比率定為1.005之外,其他與實施例Y1相同進行聚醯亞胺粉體(b-2)的合成,而得到由重量平均分子量為292,000g/mol之聚醯亞胺所構成之聚醯亞胺粉體(b-2)。(Example Y5) Except that the usage amount of 6FDA used in the synthesis of the polyimide powder (b-2) is not 89.204g (0.2008 mol), but 89.293 g (0.2010 mol), The polyimide powder (b-2) was synthesized in the same manner as in Example Y1 except that the molar ratio of the tetracarboxylic dianhydride/aromatic diamine compound was set to 1.005, and the result was obtained with a weight-average molecular weight of Polyimide powder (b-2) composed of 292,000 g/mol of polyimide.

其次,將實施例Y1所得之重量平均分子量195,000 g/mol的聚醯亞胺粉體(a-2)10g與本實施例之重量平均分子量為292,000g/mol的聚醯亞胺粉體(b-2)30g,置入回轉型之混合裝置耗費1小時以上充分混合,而得到聚醯亞胺粉體(a-2)/聚醯亞胺粉體(b-2)的重量比率為25/75之聚醯亞胺粉體。Next, 10 g of the polyimide powder (a-2) with a weight average molecular weight of 195,000 g/mol obtained in Example Y1 and the polyimide powder (b) with a weight average molecular weight of 292,000 g/mol obtained in this example -2) 30g, put it into a rotary type mixing device and spend more than 1 hour to mix thoroughly, and the weight ratio of the obtained polyimide powder (a-2)/polyimide powder (b-2) is 25/ 75 of polyimide powder.

對於所得之聚醯亞胺粉體所測定之重量平均分子量為268,000g/mol,平均粒徑為0.09mm。The weight average molecular weight measured for the obtained polyimide powder was 268,000 g/mol, and the average particle diameter was 0.09 mm.

以下,與實施例X1同樣進行所作成之50μm厚度的聚醯亞胺薄膜的全光線透過率高至90%,黃色度為1.3,即使目視亦未觀察到變色,係透明性極為優異者。又,聚醯亞胺薄膜的拉伸強度為158MPa,伸長度為68%。Hereinafter, the polyimide film with a thickness of 50 μm produced in the same manner as in Example X1 had a high total light transmittance of 90%, a yellowness of 1.3, and no discoloration was observed even by visual inspection, which was extremely excellent in transparency. In addition, the tensile strength of the polyimide film was 158 MPa, and the elongation was 68%.

(實施例Y6)   除了將聚醯亞胺粉體(a-2)的合成所使用之DMAC的使用量並非定為461g而是定為485g,作為芳香族二胺化合物,取代TFMB64.047g(0.2000莫耳),改使用TFMB51.238g (0.1600莫耳)及2,2-雙[4-(4-胺基苯氧基)苯基]-1,1,1,3,3,3-六氟丙烷(BAPP-F)20.738g(0.0400莫耳),進行化學醯亞胺化反應前所使用之稀釋用DMAC的使用量並非定為410g而是定為431g之外,其他與實施例Y1相同進行聚醯亞胺粉體(a-2)的合成,作為芳香族二胺化合物,得到TFMB以及BAPP-F,以及作為四羧酸二酐,得到由使用6FDA所合成之重量平均分子量為205,000g/mol之聚醯亞胺所構成的聚醯亞胺粉體(a-2)。(Example Y6) Except that the amount of DMAC used in the synthesis of the polyimide powder (a-2) was not 461 g but 485 g, as an aromatic diamine compound, substituted TFMB64.047 g (0.2000 g) mol), use TFMB51.238g (0.1600 mol) and 2,2-bis[4-(4-aminophenoxy)phenyl]-1,1,1,3,3,3-hexafluoro Propane (BAPP-F) 20.738g (0.0400mol), the amount of DMAC used for dilution before the chemical imidization reaction was not set at 410g but set at 431g, the other was carried out in the same way as in Example Y1 Synthesis of polyimide powder (a-2), as aromatic diamine compound, obtained TFMB and BAPP-F, and as tetracarboxylic dianhydride, obtained by using 6FDA synthesis weight average molecular weight of 205,000g/ Polyimide powder (a-2) composed of mol of polyimide.

將所得之重量平均分子量為205,000g/mol的聚醯亞胺粉體(a-2)20g與於實施例Y1所得之重量平均分子量342,000g/mol的聚醯亞胺粉體(b-2)20g,置入回轉型之混合裝置耗費1小時以上充分混合,而得到聚醯亞胺粉體(a-2)/聚醯亞胺粉體(b-2)的重量比率為50/50之聚醯亞胺粉體。20 g of the obtained polyimide powder (a-2) with a weight average molecular weight of 205,000 g/mol and the polyimide powder (b-2) with a weight average molecular weight of 342,000 g/mol obtained in Example Y1 20g, put it into the mixing device of the rotary type and spend more than 1 hour to mix thoroughly, and obtain the polyimide powder (a-2)/polyimide powder (b-2) with a weight ratio of 50/50. Imide powder.

對於所得之聚醯亞胺粉體所測定之重量平均分子量為261,000g/mol,平均粒徑為0.10mm。The weight average molecular weight measured for the obtained polyimide powder was 261,000 g/mol, and the average particle diameter was 0.10 mm.

以下,與實施例X1同樣進行所作成之50μm厚度的聚醯亞胺薄膜的全光線透過率高至89%,黃色度為1.4,即使目視亦未觀察到變色,係透明性極為優異者。又,聚醯亞胺薄膜的拉伸強度為150MPa,伸長度為60%。Hereinafter, the polyimide film with a thickness of 50 μm produced in the same manner as in Example X1 had a high total light transmittance of 89%, a yellowness of 1.4, and no discoloration was observed even by visual observation, which was extremely excellent in transparency. In addition, the tensile strength of the polyimide film was 150 MPa, and the elongation was 60%.

(實施例Y7)   作成聚醯亞胺塗料A與聚醯亞胺塗料B,該聚醯亞胺塗料A係將於實施例Y1所得之重量平均分子量195,000g/mol的聚醯亞胺粉體(a-2)20g溶解在80g之DMAC,該聚醯亞胺塗料B係將於實施例Y1所得之重量平均分子量為342,000g/mol的聚醯亞胺粉體(b-2)20g溶解在80g之DMAC,混合聚醯亞胺塗料A50g(溶解溶質之聚醯亞胺粉體(a-2)10g)與聚醯亞胺塗料B50g(溶解溶質之聚醯亞胺粉體(b-2)10g),而得到作為目的之聚醯亞胺塗料。(Example Y7) A polyimide coating A and a polyimide coating B were prepared. The polyimide coating A is a polyimide powder with a weight-average molecular weight of 195,000 g/mol obtained in Example Y1 ( a-2) 20g is dissolved in 80g of DMAC, the polyimide coating B is to dissolve 20g of the polyimide powder with a weight average molecular weight of 342,000g/mol obtained in Example Y1 (b-2) in 80g DMAC, mixed polyimide coating A50g (polyimide powder (a-2) 10g dissolved solute) and polyimide coating B50g (polyimide powder (b-2) 10g dissolved solute) ) to obtain the intended polyimide coating.

溶解在所得之聚醯亞胺塗料中之聚醯亞胺的重量平均分子量為259,000g/mol。The weight average molecular weight of the polyimide dissolved in the obtained polyimide coating material was 259,000 g/mol.

以下,與實施例Y1同樣進行所作成之50μm厚度的聚醯亞胺薄膜的全光線透過率高至90%,黃色度為1.3,即使目視亦未觀察到變色,係透明性極為優異者。又,聚醯亞胺薄膜的拉伸強度為165MPa,伸長度為70%。Hereinafter, the polyimide film with a thickness of 50 μm produced in the same manner as in Example Y1 had a high total light transmittance of 90%, a yellowness of 1.3, and no discoloration was observed even by visual observation, which was extremely excellent in transparency. In addition, the tensile strength of the polyimide film was 165 MPa, and the elongation was 70%.

(比較例Y1)   僅將於實施例Y1合成之重量平均分子量195,000g/mol的聚醯亞胺粉體(a-2)20g溶解在80g之DMAC,而成為均一之聚醯亞胺溶液後,使用施用器塗膜在玻璃板上,以指定的條件乾燥DMAC後,從玻璃板剝離作成50μm厚度的聚醯亞胺薄膜時,成為所得之聚醯亞胺薄膜的全光線透過率為89%,黃色度為1.8,拉伸強度為125MPa,伸長度為20%之低的結果。(Comparative Example Y1) Only after dissolving 20 g of the polyimide powder (a-2) with a weight average molecular weight of 195,000 g/mol synthesized in Example Y1 in 80 g of DMAC to obtain a uniform polyimide solution, After coating the film on a glass plate with an applicator, drying DMAC under the specified conditions, and peeling off the glass plate to make a polyimide film with a thickness of 50 μm, the total light transmittance of the obtained polyimide film is 89%. The yellowness was 1.8, the tensile strength was 125 MPa, and the elongation was as low as 20%.

(比較例Y2)   僅將於實施例Y1合成之重量平均分子量342,000g/mol的聚醯亞胺粉體(b-2)20g溶解在80g之DMAC時,聚醯亞胺塗料的黏度過高,難以成為適合塗膜之黏度的塗料。因此,進而追加60gDMAC作為12.5%之塗料後,使用施用器塗膜在玻璃板上,以指定的條件乾燥DMAC後,從玻璃板剝離作成50μm厚度的聚醯亞胺薄膜。所得之聚醯亞胺薄膜的全光線透過率雖為90%,黃色度1.3,但拉伸強度為145MPa,伸長度為40%時,與上述實施例Y比較,成為較低的結果。(Comparative Example Y2) Only when 20 g of polyimide powder (b-2) with a weight average molecular weight of 342,000 g/mol synthesized in Example Y1 was dissolved in 80 g of DMAC, the viscosity of the polyimide coating was too high, It is difficult to make a coating suitable for the viscosity of the coating film. Therefore, after further adding 60 g of DMAC as a 12.5% coating material, the film was coated on a glass plate using an applicator, and after drying DMAC under the specified conditions, it was peeled off from the glass plate to prepare a polyimide film with a thickness of 50 μm. Although the total light transmittance of the obtained polyimide film was 90% and the yellowness was 1.3, when the tensile strength was 145 MPa and the elongation was 40%, compared with the above-mentioned Example Y, the results were lower.

將結果集中於表2。

Figure 02_image003
[產業上之可利用性]The results are gathered in Table 2.
Figure 02_image003
[Industrial Availability]

若使用有關本發明之聚醯亞胺粉體或聚醯亞胺塗料,可製造可兼具極為優異之耐熱性、機械特性及透明性,尤其是適合使用在顯示器用途或電子材料用途的聚醯亞胺薄膜,產業上的價值極高。If the polyimide powder or polyimide coating according to the present invention is used, it is possible to manufacture polyimide having excellent heat resistance, mechanical properties and transparency, especially suitable for use in displays or electronic materials. The imine film has extremely high industrial value.

Claims (11)

一種聚醯亞胺粉體,其係由聚醯亞胺粉體A與聚醯亞胺粉體B的混合所構成,且為可溶於有機溶媒的聚醯亞胺粉體,其特徵為聚醯亞胺粉體A及聚醯亞胺粉體B,分別由具有源自至少1種類的芳香族二胺化合物之構造單位與源自至少1種類四羧酸二酐之構造單位的聚醯亞胺所構成,於前述至少1種類的芳香族二胺化合物,包含至少1種類具有氟基之芳香族二胺化合物,於前述至少1種類的四羧酸二酐,包含至少1種類具有氟基之芳香族四羧酸二酐,聚醯亞胺粉體A係由具有(a-1)1.2dL/g以上且未滿2.1dL/g之還原黏度的聚醯亞胺所構成,聚醯亞胺粉體B係由具有(b-1)2.1dL/g以上3.0dL/g以下之還原黏度的聚醯亞胺所構成,前述聚醯亞胺粉體A/聚醯亞胺粉體B的重量比為10/90~90/10的範圍,對於聚醯亞胺粉體A與聚醯亞胺粉體B的混合所測定之還原黏度為1.7~2.5dL/g的範圍。 A polyimide powder, which is composed of a mixture of polyimide powder A and polyimide powder B, and is a polyimide powder soluble in organic solvents, characterized by a polyimide powder. Imide powder A and polyimide powder B, each composed of a polyimide having a structural unit derived from at least one type of aromatic diamine compound and a structural unit derived from at least one type of tetracarboxylic dianhydride Consists of amines, at least one kind of aromatic diamine compound, including at least one kind of aromatic diamine compound having a fluorine group, and at least one kind of tetracarboxylic dianhydride, including at least one kind of fluorine group. Aromatic tetracarboxylic dianhydride, polyimide powder A is composed of polyimide having a reducing viscosity of (a-1) 1.2dL/g or more and less than 2.1dL/g, polyimide Powder B is composed of (b-1) polyimide having a reducing viscosity of not less than 2.1 dL/g and not more than 3.0 dL/g, and the weight of the aforementioned polyimide powder A/polyimide powder B The ratio is in the range of 10/90 to 90/10, and the reduced viscosity measured for the mixture of the polyimide powder A and the polyimide powder B is in the range of 1.7 to 2.5 dL/g. 一種聚醯亞胺粉體,其係由聚醯亞胺粉體A與聚醯亞胺粉體B的混合所構成,且為可溶於有機溶媒的聚醯亞胺粉體,其特徵為聚醯亞胺粉體A及聚醯亞胺粉體B,分別 由具有源自至少1種類的芳香族二胺化合物之構造單位與源自至少1種類四羧酸二酐之構造單位的聚醯亞胺所構成,於前述至少1種類的芳香族二胺化合物,包含至少1種類具有氟基之芳香族二胺化合物,於前述至少1種類的四羧酸二酐,包含至少1種類具有氟基之芳香族四羧酸二酐,聚醯亞胺粉體A係由具有(a-2)100,000g/mol以上且未滿250,000g/mol之重量平均分子量的聚醯亞胺所構成,聚醯亞胺粉體B係由具有(b-2)250,000g/mol以上500,000g/mol以下之重量平均分子量的聚醯亞胺所構成,前述聚醯亞胺粉體A/聚醯亞胺粉體B的重量比為10/90~90/10的範圍,對於聚醯亞胺粉體A與聚醯亞胺粉體B的混合所測定之重量平均分子量為160,000~350,000g/mol的範圍。 A polyimide powder, which is composed of a mixture of polyimide powder A and polyimide powder B, and is a polyimide powder soluble in organic solvents, characterized by a polyimide powder. Imide powder A and polyimide powder B, respectively Consisting of a polyimide having a structural unit derived from at least one type of aromatic diamine compound and a structural unit derived from at least one type of tetracarboxylic dianhydride, in the at least one type of aromatic diamine compound, Contains at least one kind of aromatic diamine compound having fluorine group, at least one kind of tetracarboxylic dianhydride described above, contains at least one kind of aromatic tetracarboxylic dianhydride having fluorine group, polyimide powder A series It is composed of polyimide having a weight average molecular weight of (a-2) 100,000 g/mol or more and less than 250,000 g/mol, and the polyimide powder B is composed of (b-2) 250,000 g/mol It is composed of polyimide with a weight average molecular weight of 500,000 g/mol or less, and the weight ratio of the polyimide powder A/polyimide powder B is in the range of 10/90 to 90/10. The weight average molecular weight measured by mixing the imide powder A and the polyimide powder B is in the range of 160,000 to 350,000 g/mol. 如請求項1或2之聚醯亞胺粉體,其中,聚醯亞胺粉體A與聚醯亞胺粉體B係由具有源自同一芳香族二胺化合物之構造單位與源自同一四羧酸二酐之構造單位的聚醯亞胺所構成。 The polyimide powder according to claim 1 or 2, wherein the polyimide powder A and the polyimide powder B are composed of structural units derived from the same aromatic diamine compound and derived from the same It is composed of polyimide which is the structural unit of tetracarboxylic dianhydride. 如請求項1或2之聚醯亞胺粉體,其中,聚醯亞胺粉體A及聚醯亞胺粉體B皆為由經由對聚醯胺酸之聚合、化學醯亞胺化反應、生成聚醯亞胺的析出所致之粉體的形成及 乾燥之步驟所製造之聚醯亞胺所構成。 As claimed in claim 1 or 2, the polyimide powder, wherein, the polyimide powder A and the polyimide powder B are both obtained through the polymerization of polyimide, chemical imidization reaction, Formation of powder due to precipitation of polyimide and It consists of the polyimide produced in the drying step. 如請求項1或2之聚醯亞胺粉體,其中,前述對於聚醯亞胺粉體A與聚醯亞胺粉體B的混合所測定之平均粒徑為0.02~0.8mm的範圍。 The polyimide powder according to claim 1 or 2, wherein the average particle size measured for the mixture of the polyimide powder A and the polyimide powder B is in the range of 0.02 to 0.8 mm. 如請求項1或2之聚醯亞胺粉體,其中,從溶解在有機溶媒之溶液進行製膜所得之厚度50μm的聚醯亞胺薄膜,給予85%以上之全光線透過率及-3~3的範圍之黃色度(Yellow Index)。 The polyimide powder of claim 1 or 2, wherein the polyimide film with a thickness of 50 μm obtained from a solution dissolved in an organic solvent for film formation has a total light transmittance of 85% or more and a total light transmittance of -3~ Yellowness in the range of 3 (Yellow Index). 一種聚醯亞胺塗料,其特徵為於有機溶媒中,如請求項1~6中任一項之聚醯亞胺粉體以1~30重量%的濃度溶解。 A polyimide coating is characterized in that in an organic solvent, the polyimide powder according to any one of claims 1 to 6 is dissolved at a concentration of 1 to 30% by weight. 一種聚醯亞胺塗料的製造方法,其係包含將聚醯亞胺粉體A以成為1~30重量%的濃度的方式溶解在有機溶媒的塗料、與將聚醯亞胺粉體B以成為1~30重量%的濃度的方式溶解在有機溶媒的塗料以聚醯亞胺粉體A/聚醯亞胺粉體B的重量比成為10/90~90/10的範圍的方式混合,該聚醯亞胺粉體A係由具有源自至少1種類的芳香族二胺化合物之構造單位與源自至少1種類四羧酸二酐之構造單位,且可溶於有機溶媒的具有(a-1)1.2dL/g以上且未滿2.1dL/g之還原黏度的聚醯亞胺所構成,該聚醯亞胺粉體B係由具有源 自至少1種類的芳香族二胺化合物之構造單位與源自至少1種類四羧酸二酐之構造單位,且可溶於有機溶媒的具有(b-1)2.1dL/g以上3.0dL/g以下之還原黏度的聚醯亞胺所構成,於前述至少1種類的芳香族二胺化合物,包含至少1種類具有氟基之芳香族二胺化合物,於前述至少1種類的四羧酸二酐,包含至少1種類具有氟基之芳香族四羧酸二酐。 A method for producing a polyimide paint, comprising: dissolving polyimide powder A in an organic solvent at a concentration of 1 to 30 wt %; and dissolving polyimide powder B in a manner of The paint dissolved in the organic solvent at a concentration of 1 to 30% by weight is mixed so that the weight ratio of the polyimide powder A/polyimide powder B is in the range of 10/90 to 90/10, and the polyimide powder is mixed. The imide powder A is composed of a structural unit derived from at least one type of aromatic diamine compound and a structural unit derived from at least one type of tetracarboxylic dianhydride, and is soluble in an organic solvent and has (a-1 ) 1.2dL/g or more and less than 2.1dL/g of polyimide with a reduced viscosity, the polyimide powder B is composed of A structural unit derived from at least one kind of aromatic diamine compound and a structural unit derived from at least one kind of tetracarboxylic dianhydride, and having (b-1) 2.1 dL/g or more 3.0 dL/g soluble in organic solvent The following polyimide with reduced viscosity is composed of at least one type of aromatic diamine compound, at least one type of aromatic diamine compound having a fluorine group, and at least one type of tetracarboxylic dianhydride, At least one kind of aromatic tetracarboxylic dianhydride having a fluorine group is contained. 一種聚醯亞胺塗料的製造方法,其係包含將聚醯亞胺粉體A以成為1~30重量%的濃度的方式溶解在有機溶媒的塗料、與將聚醯亞胺粉體B以成為1~30重量%的濃度的方式溶解在有機溶媒的塗料以聚醯亞胺粉體A/聚醯亞胺粉體B的重量比成為10/90~90/10的範圍的方式混合,該聚醯亞胺粉體A係由具有源自至少1種類的芳香族二胺化合物之構造單位與源自至少1種類四羧酸二酐之構造單位,且可溶於有機溶媒的具有(a-2)100,000g/mol以上且未滿250,000g/mol之重量平均分子量的聚醯亞胺所構成,該聚醯亞胺粉體B係具有源自至少1種類的芳香族二胺化合物之構造單位與源自至少1種類四羧酸二酐之構造單位,且可溶於有機溶媒的具有(b-2)100,000g/mol以上且未滿250,000g/mol之重量平均分子量的聚醯亞胺所構成,於前述至少1種類的芳香族二胺化合物,包含至少1種類具有氟基之芳香族二胺化合物, 於前述至少1種類的四羧酸二酐,包含至少1種類具有氟基之芳香族四羧酸二酐。 A method for producing a polyimide paint, comprising: dissolving polyimide powder A in an organic solvent at a concentration of 1 to 30 wt %; and dissolving polyimide powder B in a manner of The paint dissolved in the organic solvent at a concentration of 1 to 30% by weight is mixed so that the weight ratio of the polyimide powder A/polyimide powder B is in the range of 10/90 to 90/10, and the polyimide powder is mixed. The imide powder A is composed of a structural unit derived from at least one type of aromatic diamine compound and a structural unit derived from at least one type of tetracarboxylic dianhydride, and is soluble in an organic solvent and has (a-2 ) 100,000 g/mol or more and less than 250,000 g/mol of polyimide having a weight-average molecular weight of less than 250,000 g/mol, the polyimide powder B having a structural unit derived from at least one kind of aromatic diamine compound and Consists of (b-2) Polyimide having a weight average molecular weight of 100,000 g/mol or more and less than 250,000 g/mol, which is derived from at least one structural unit of tetracarboxylic dianhydride and is soluble in organic solvents , in the aforementioned at least one kind of aromatic diamine compound, including at least one kind of aromatic diamine compound having a fluorine group, At least 1 type of aromatic tetracarboxylic dianhydride having a fluorine group is included in the at least 1 type of tetracarboxylic dianhydride. 一種聚醯亞胺薄膜,其係製膜如請求項7之聚醯亞胺塗料所得。 A polyimide film, which is obtained by film-making as the polyimide coating of claim 7. 如請求項10之聚醯亞胺薄膜,其中,全光線透過率為85%以上,且黃色度為-3~3的範圍。 The polyimide film of claim 10, wherein the total light transmittance is 85% or more, and the yellowness is in the range of -3 to 3.
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