TW201629123A - Porous polyimide film and production method thereof - Google Patents

Porous polyimide film and production method thereof Download PDF

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TW201629123A
TW201629123A TW104143196A TW104143196A TW201629123A TW 201629123 A TW201629123 A TW 201629123A TW 104143196 A TW104143196 A TW 104143196A TW 104143196 A TW104143196 A TW 104143196A TW 201629123 A TW201629123 A TW 201629123A
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porous
film
solvent
less
porosity
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山田宗紀
柴田健太
竹內耕
吉野文子
藤岡直史
繁田朗
越後良彰
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尤尼吉可股份有限公司
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/28Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof by elimination of a liquid phase from a macromolecular composition or article, e.g. drying of coagulum
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G73/00Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
    • C08G73/06Polycondensates having nitrogen-containing heterocyclic rings in the main chain of the macromolecule
    • C08G73/10Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors
    • C08G73/1046Polyimides containing oxygen in the form of ether bonds in the main chain
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L79/00Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen or carbon only, not provided for in groups C08L61/00 - C08L77/00
    • C08L79/04Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
    • C08L79/08Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors

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  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
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  • Manufacturing & Machinery (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The present invention provides a porous polyimide film having a high porosity and a small average pore diameter, in which no porogen and the like are remaining, and a production method thereof. A porous polyimide film of the present invention is characterized by comprising a polyimide containing an oxyalkylene unit and having a porosity of 45 vol% or more to 95 vol% or less and an average pore diameter of 10 nm or more to 1000 nm or less.

Description

多孔質聚醯亞胺薄膜及其製造方法 Porous polyimine film and manufacturing method thereof

本發明係關於多孔質聚醯亞胺(PI)薄膜及其製造方法。 The present invention relates to a porous polyimine (PI) film and a method for producing the same.

多孔質PI薄膜利用其優異耐熱性與高氣孔率,而被利用於例如:電子材料、光學材料、鋰二次電池用隔板、過濾器、分離膜、電線被覆等產業用材料、醫療材料的素材等領域。就製造該多孔質PI薄膜的方法,在專利文獻1~3中有提案:將含有對PI(包括其前驅物在內)呈良溶劑及不良溶劑的PI溶液,塗佈於基材上,經乾燥而獲得多孔質PI薄膜的方法(以下,將該方法簡稱「乾式多孔化程序」)。 The porous PI film is used for industrial materials such as electronic materials, optical materials, separators for lithium secondary batteries, filters, separation membranes, and wire coatings, and medical materials, because of its excellent heat resistance and high porosity. Materials and other fields. In the method of producing the porous PI thin film, Patent Documents 1 to 3 propose that a PI solution containing a good solvent and a poor solvent for PI (including its precursor) is applied onto a substrate. A method of obtaining a porous PI film by drying (hereinafter, this method is simply referred to as "dry porous process").

乾式多孔化程序在製造多孔質PI薄膜時,與將基材上所形成的塗膜浸漬於含不良溶劑的凝固液中,而達多孔質化的濕式多孔化程序不同,並不需要為了多孔質化而使用凝固浴。所以,因為乾式多孔化程序在多孔質PI薄膜製造時,不會從凝固浴產生廢液,因而屬於環境相容性佳的優異方法。然而,利用乾式多孔程序獲得的多孔質PI薄膜,多屬平均氣孔徑達1000nm以上之情況,頗難將其製成未滿1000nm。就獲得平均氣孔徑未滿1000nm多孔質PI薄膜 的方法,在專利文獻4有提案:在PI薄膜中,將熱分解溫度為350℃以下的熱分解性有機化合物作為造孔劑使用(氣孔形成劑)來形成氣孔,而製造多孔質PI薄膜的方法。此種專利文獻4所記載的方法,係將造孔劑摻合於PI薄膜中而獲得PI薄膜之後,再將上述熱分解性有機化合物於350℃以上的溫度施行長時間熱處理,將上述熱分解性有機化合物施行熱分解而使之消失並除去,藉此形成氣孔。又,專利文獻5有提案:將聚乙二醇單甲基丙烯酸酯等分散性化合物作為造孔劑使用,使氣孔形成而製造多孔質PI薄膜的方法。此種專利文獻5所記載的方法,係將造孔劑摻合於PI薄膜中而獲得PI薄膜之後,再利用超臨界二氧化碳萃取除去造孔劑而使氣孔形成。 The dry-type porous process is different from the wet-type porous process in which the porous film is formed by immersing the coating film formed on the substrate in a coagulating liquid containing a poor solvent, and is not required to be porous. The coagulation bath is used for the quality. Therefore, since the dry porous process does not generate waste liquid from the coagulation bath when the porous PI film is produced, it is an excellent method with good environmental compatibility. However, the porous PI film obtained by the dry porous procedure mostly has an average pore diameter of 1000 nm or more, and it is difficult to make it less than 1000 nm. Obtain a porous PI film with an average pore diameter of less than 1000 nm In the case of the PI film, a thermally decomposable organic compound having a thermal decomposition temperature of 350 ° C or less is used as a pore-forming agent (a pore forming agent) to form pores, and a porous PI film is produced. method. In the method described in Patent Document 4, after the PI film is obtained by blending a pore former in a PI film, the pyrolytic organic compound is subjected to a long-time heat treatment at a temperature of 350 ° C or higher to thermally decompose the above. The organic compound is thermally decomposed to disappear and removed, thereby forming pores. Further, Patent Document 5 proposes a method of producing a porous PI film by using a dispersing compound such as polyethylene glycol monomethacrylate as a pore-forming agent and forming pores. In the method described in Patent Document 5, a pore former is blended into a PI film to obtain a PI film, and then a pore former is removed by supercritical carbon dioxide extraction to form pores.

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

[專利文獻1]日本專利第4947989號公報 [Patent Document 1] Japanese Patent No. 4947989

[專利文獻2]日本專利特開2015-136633號公報 [Patent Document 2] Japanese Patent Laid-Open No. 2015-136633

[專利文獻3]日本專利特開2015-52061號公報 [Patent Document 3] Japanese Patent Laid-Open Publication No. 2015-52061

[專利文獻4]日本專利特開2013-216776號公報 [Patent Document 4] Japanese Patent Laid-Open Publication No. 2013-216776

[專利文獻5]日本專利第4557409號公報 [Patent Document 5] Japanese Patent No. 4557409

然而,使用熱分解性有機化合物及分散性化合物等造孔劑的習知方法,具有所使用造孔劑未被完全除去而殘留於多孔質PI薄膜 中,導致損及多孔質PI薄膜之耐熱性及力學強度的問題。 However, a conventional method using a pore-forming agent such as a thermally decomposable organic compound or a dispersing compound has a pore-forming agent which is not completely removed and remains in the porous PI film. Among them, there is a problem that the heat resistance and mechanical strength of the porous PI film are impaired.

有鑑於此,本發明係為解決上述問題而完成,目的在於提供:具有高氣孔率與較小平均氣孔徑,且不會殘留造孔劑等的多孔質PI薄膜及其製造方法。 In view of the above, the present invention has been made to solve the above problems, and an object thereof is to provide a porous PI film having a high porosity and a small average pore diameter without leaving a pore former or the like and a method for producing the same.

本發明者等發現藉由將PI的化學構造設為特定組成,且將多孔質薄膜的氣孔構造設為特定構造,便可解決上述問題,遂完成本發明。 The inventors of the present invention have found that the above problems can be solved by setting the chemical structure of PI to a specific composition and the pore structure of the porous film to have a specific structure, and have completed the present invention.

本發明主旨係如下述。 The gist of the present invention is as follows.

<1>一種多孔質聚醯亞胺薄膜,其特徵在於,由含氧化伸烷基單元的聚醯亞胺構成,氣孔率係45體積%以上且95體積%以下,平均氣孔徑係10nm以上且1000nm以下。 <1> A porous polyimide film comprising a polyalkylenimine containing an alkylene oxide unit, having a porosity of 45 vol% or more and 95 vol% or less, and an average pore diameter of 10 nm or more. Below 1000nm.

<2>如上述多孔質聚醯亞胺薄膜,其中,在表面上形成活性層。 <2> The above porous polyimine film, wherein an active layer is formed on the surface.

<3>一種多孔質聚醯亞胺薄膜之製造方法,其特徵在於,將由含氧化伸烷基單元之聚醯胺酸、與含其良溶劑與不良溶劑的混合溶劑構成,且上述混合溶劑中的不良溶劑比率係65質量%以上且95質量%以下的溶液,塗佈於基材上之後,依未滿350℃的溫度施行乾燥。 <3> A method for producing a porous polyimine film, which comprises a polyphthalic acid containing an alkylene oxide unit and a mixed solvent containing a good solvent and a poor solvent, and the mixed solvent The solution having a poor solvent ratio of 65 mass% or more and 95 mass% or less is applied to the substrate, and then dried at a temperature of less than 350 °C.

本發明之多孔質PI薄膜,因為耐熱性優異、氣孔率高、且不會殘留造孔劑等氣孔形成劑,因而頗適用於例如:低介電常數基板等電子材料、鋰二次電池用隔板、燃料電池的固體電解質負載膜、過濾器、分離膜、電線被覆等產業用材料、醫療材料、光學材料的素材等。 The porous PI film of the present invention is excellent in heat resistance, high in porosity, and does not leave a pore forming agent such as a pore former, and is therefore suitably used for, for example, an electronic material such as a low dielectric constant substrate or a lithium secondary battery separator. Industrial materials such as plates, fuel cell solid electrolyte supporting membranes, filters, separation membranes, and wire coatings, materials for medical materials, and optical materials.

圖1係實施例1所獲得多孔質PI薄膜(P-1)截面的SEM影像。 Fig. 1 is a SEM image of a cross section of a porous PI film (P-1) obtained in Example 1.

圖2係實施例1所獲得多孔質PI薄膜(P-1)表面的SEM影像。 2 is an SEM image of the surface of the porous PI film (P-1) obtained in Example 1.

圖3係比較例1所獲得多孔質PI薄膜(R-1)截面的SEM影像。 3 is an SEM image of a cross section of a porous PI film (R-1) obtained in Comparative Example 1.

以下,針對本發明進行詳細說明。 Hereinafter, the present invention will be described in detail.

本發明係關於多孔質PI薄膜及其製造方法。 The present invention relates to a porous PI film and a method for producing the same.

此處,PI(聚醯亞胺)係主鏈具有醯亞胺鍵的耐熱性高分子,通常係藉由單體成分之二胺成分與四羧酸成分進行聚縮合而獲得。該等聚醯亞胺亦包括屬於聚醯亞胺改質體的聚醯胺醯亞胺、聚酯醯亞胺等。 Here, the PI (polyimine)-based heat-resistant polymer having a quinone bond in the main chain is usually obtained by polycondensation of a diamine component of a monomer component and a tetracarboxylic acid component. The polyimines also include polyamidoximines, polyesterimines, and the like which are polyimine modified bodies.

PI最好係使用由屬於聚醯亞胺前驅物之聚醯胺酸(以下簡稱「PAA」)獲得的PI。此情況,PI薄膜係藉由將由溶劑中使四羧酸二酐與二胺進行反應而獲得的PAA溶液塗佈於基材上,於形成PAA被膜後,再以熱性或化學性方式將PAA施行醯亞胺化便可獲得。 由PAA所獲得的PI係可為熱可塑性、亦可為非熱可塑性。 Preferably, PI is a PI obtained from polyglycine (hereinafter referred to as "PAA") which is a polyimide precursor. In this case, the PI film is applied to the substrate by reacting a PAA solution obtained by reacting a tetracarboxylic dianhydride with a diamine in a solvent to form a PAA film, and then performing PAA thermally or chemically. The imidization can be obtained. The PI system obtained from PAA may be thermoplastic or non-thermoplastic.

本發明的PI係含有氧化伸烷基單元。氧化伸烷基單元具體係可例如:氧化伸乙基單元、氧化伸丙基單元、氧化伸丁基單元等。含氧化伸烷基單元的PI係例如藉由將具氧化伸烷基單元的四羧酸二酐(以下簡稱「TA-1」)及/或具氧化伸烷基單元的二胺(以下簡稱「DA-1」),與未具氧化伸烷基單元的四羥酸二酐(以下簡稱「TA-2」)及/或未具氧化伸烷基單元的二胺(以下簡稱「DA-2」)進行共聚合的PAA(以下簡稱「共聚合PAA」),施行醯亞胺化便可獲得。藉由將此種氧化伸烷基單元導入於PI鏈(主鏈)中,便可依乾式多孔化程序形成具有平均氣孔徑在1000nm以下之微細氣孔的多孔質PI薄膜。相關上述單體的具體例及共聚合比率等,容待後述。 The PI system of the present invention contains an alkylene oxide unit. The alkylene oxide unit may specifically be, for example, an oxidized ethyl group unit, an oxidized propyl unit, an oxybutylene unit or the like. The PI containing an alkylene oxide unit is, for example, a tetracarboxylic dianhydride having an oxidized alkyl unit (hereinafter referred to as "TA-1") and/or a diamine having an alkylene oxide unit (hereinafter referred to as " DA-1"), with a tetrahydroxy acid dianhydride (hereinafter referred to as "TA-2") having no alkylene oxide unit and/or a diamine having no alkylene oxide unit (hereinafter referred to as "DA-2") The PAA (hereinafter referred to as "copolymerized PAA") which is subjected to copolymerization can be obtained by performing imidization. By introducing such an alkylene oxide unit into the PI chain (backbone), a porous PI film having fine pores having an average pore diameter of 1000 nm or less can be formed by a dry pore-forming procedure. Specific examples of the above-mentioned monomers, copolymerization ratios, and the like are to be described later.

本發明多孔質PI薄膜的氣孔率係45體積%以上且95體積%以下、較佳係50體積%以上且90體積%以下、更佳係55體積%以上且85體積%以下。藉由將氣孔率設定為此種範圍,便可同時確保成為多孔質薄膜時的良好機械特性、優異穿透性、及介電特性等。 The porosity of the porous PI film of the present invention is 45 vol% or more and 95 vol% or less, preferably 50 vol% or more and 90 vol% or less, more preferably 55 vol% or more and 85% by volume or less. By setting the porosity to such a range, it is possible to simultaneously ensure good mechanical properties, excellent penetrability, dielectric properties, and the like when the porous film is formed.

氣孔率係可使用利用下式計算出的值。 The porosity ratio can be a value calculated by the following formula.

[數式1]氣孔率(體積%)=100-100×(W/D)/(S×T) [Formula 1] Porosity (% by volume) = 100 - 100 × (W / D) / (S × T)

式中的S表示多孔質PI薄膜的面積,T表示厚度,W表示質量,D表示所對應非多孔質PI薄膜的密度。 In the formula, S represents the area of the porous PI film, T represents the thickness, W represents the mass, and D represents the density of the corresponding non-porous PI film.

本發明之多孔質PI薄膜的平均氣孔徑為10nm以上且1000nm以下、較佳為20nm以上且800nm以下、更佳為20nm以上且600nm以下。藉由將平均氣孔徑設為此種範圍,便可同時確保成為多孔質薄膜時的良好機械特性、優異穿透性、及介電特性等 The porous PI film of the present invention has an average pore diameter of 10 nm or more and 1000 nm or less, preferably 20 nm or more and 800 nm or less, more preferably 20 nm or more and 600 nm or less. By setting the average pore diameter to such a range, it is possible to simultaneously ensure good mechanical properties, excellent penetrability, dielectric properties, and the like when the porous film is used.

平均氣孔徑係依倍率5000~20000倍取得多孔質PI薄膜截面的SEM(掃描式電子顯微鏡)影像,再藉由利用影像處理軟體進行分析便可確認。 The average pore diameter is obtained by SEM (scanning electron microscope) image of the cross section of the porous PI film at a magnification of 5,000 to 20,000 times, and can be confirmed by analysis using an image processing software.

本發明多孔質PI薄膜的氣孔係可為連續氣孔、亦可為獨立氣孔。 The pore system of the porous PI film of the present invention may be a continuous pore or an independent pore.

本發明多孔質PI薄膜的表面係可呈開口、亦可未呈開口。 The surface of the porous PI film of the present invention may or may not be open.

有呈開口時的開口率較佳為10%以上且90%以下、更佳為20%以上且80%以下。又,呈開口氣孔的平均開口徑較佳係10nm以上且1000nm以下。 The opening ratio at the time of opening is preferably 10% or more and 90% or less, more preferably 20% or more and 80% or less. Further, the average opening diameter of the open pores is preferably 10 nm or more and 1000 nm or less.

藉此,可同時確保成為經開口多孔質薄膜的良好機械特性、與良好表面平滑性。 Thereby, it is possible to ensure good mechanical properties and good surface smoothness of the open porous film at the same time.

開口率及平均開口徑係依倍率5000~20000倍取得多孔質PI薄膜表面的SEM影像,再藉由利用影像處理軟體進行分析便可確認。 The aperture ratio and the average opening diameter were obtained by taking an SEM image of the surface of the porous PI film at a magnification of 5,000 to 20,000 times, and it was confirmed by analysis using an image processing software.

本發明的多孔質PI薄膜係例如可藉由以下所示乾式多孔化程序進行製造。即,將含有共聚合PAA、及其良溶劑與不良溶劑的溶 液塗佈於基材上之後,經乾燥便可製造。 The porous PI film of the present invention can be produced, for example, by the dry porosification procedure shown below. That is, it will contain a copolymerized PAA, a good solvent and a poor solvent. After the liquid is applied to the substrate, it can be produced by drying.

此處,所謂「良溶劑」係指溶質(聚醯胺酸)對溶劑質量的25℃溶解度係達1質量%以上的溶劑;所謂「不良溶劑」係指上述溶解度未滿1質量%的溶劑。良溶劑係可例如醯胺系溶劑、脲系溶劑。該等係可單獨使用、亦可組合使用2種以上。醯胺系溶劑的具體例係可例如:N-甲基-2-吡咯啶酮(NMP)、N,N-二甲基甲醯胺、N,N-二甲基乙醯胺(DMAc)等。又,脲系溶劑的具體例係可例如:四甲脲、四乙脲、二甲基伸乙脲、二甲基伸丙脲等。該等之中,較佳係NMP及DMAc。 Here, the "good solvent" means a solvent having a solubility of a solute (polyproline) to a solvent of 25 ° C of 1% by mass or more, and the term "poor solvent" means a solvent having a solubility of less than 1% by mass. The good solvent may be, for example, a guanamine solvent or a urea solvent. These may be used alone or in combination of two or more. Specific examples of the guanamine-based solvent may, for example, be N-methyl-2-pyrrolidone (NMP), N,N-dimethylformamide, N,N-dimethylacetamide (DMAc), or the like. . Further, specific examples of the urea solvent include, for example, tetramethylurea, tetraethylurea, dimethylacetamide, dimethylpropionaldehyde, and the like. Among these, NMP and DMAc are preferred.

不良溶劑係可例如醚系溶劑、醇系溶劑。該等係可單獨使用、亦可組合使用2種以上。該等之中,較佳係醚系溶劑。醚系溶劑係可例如:二乙二醇二甲醚、三乙二醇二甲醚、四乙二醇二甲醚、五乙二醇二甲醚、二乙二醇丁基甲醚、二乙二醇二乙醚、二丙二醇單甲醚等。該等係可單獨使用、亦可組合使用2種以上。該等之中,較佳係三乙二醇二甲醚及四乙二醇二甲醚。 The poor solvent may be, for example, an ether solvent or an alcohol solvent. These may be used alone or in combination of two or more. Among these, an ether solvent is preferred. The ether solvent may be, for example, diethylene glycol dimethyl ether, triethylene glycol dimethyl ether, tetraethylene glycol dimethyl ether, pentaethylene glycol dimethyl ether, diethylene glycol butyl methyl ether, diethylene glycol. Diethyl ether, dipropylene glycol monomethyl ether, and the like. These may be used alone or in combination of two or more. Among these, triethylene glycol dimethyl ether and tetraethylene glycol dimethyl ether are preferred.

不良溶劑較佳係使用沸點較良溶劑高者,沸點差較佳係達5℃以上、更佳係達20℃以上、特佳係達30℃以上。混合溶劑中的不良溶劑摻合量,較佳係將混合溶劑中的不良溶劑比率設為65質量%以上且95質量%以下、更佳係70質量%以上且90質量%以下。藉此在乾式多孔化程序的乾燥步驟中,能效率佳地引發相分離,可獲得具有高氣孔率與較小平均氣孔徑的PI薄膜。若混合溶劑中的不 良溶劑比率過少,則多孔質PI薄膜的氣孔率會降低。 The poor solvent is preferably one having a higher boiling point than the good solvent, and the difference in boiling point is preferably at least 5 ° C, more preferably at least 20 ° C, and particularly preferably at 30 ° C or higher. The amount of the poor solvent blended in the mixed solvent is preferably 65% by mass or more and 95% by mass or less, more preferably 70% by mass or more and 90% by mass or less. Thereby, phase separation can be efficiently initiated in the drying step of the dry porosification process, and a PI film having a high porosity and a small average pore diameter can be obtained. If the solvent is not mixed When the ratio of the good solvent is too small, the porosity of the porous PI film is lowered.

作為上述共聚合PAA溶液,係可使用例如由屬於單體的四羧酸二酐與二胺依略等莫耳摻合,再使該等在上述混合溶劑中進行聚合反應而獲得的溶液。此時,因為有使用四羧酸二酐的TA-1或二胺的DA-1中之至少其中一者,因而可獲得主鏈中含有氧化伸烷基單元的共聚合PAA,結果能獲得主鏈中含有氧化伸烷基單元的PI。 As the above-mentioned copolymerized PAA solution, for example, a solution obtained by subjecting a tetracarboxylic dianhydride belonging to a monomer to a molar ratio of a diamine or a diamine to a polymerization reaction in the above mixed solvent can be used. At this time, since at least one of TA-1 using a tetracarboxylic dianhydride or DA-1 of a diamine is used, a copolymerized PAA having an alkylene oxide unit in the main chain can be obtained, and as a result, a main can be obtained. The chain contains the PI of the oxyalkylene unit.

具體而言,上述共聚合PAA溶液係可使用由屬於單體的四羥酸二酐(TA-1與TA-2之混合物、或僅TA-2)、與二胺(DA-1與DA-2的混合物、或僅DA-2)依約略等莫耳摻合,使其在上述混合溶劑中以10~70℃溫度進行聚合反應而獲得的溶液。此處,使用TA-1時,TA-1的使用量就從成為更高氣孔率及更小平均氣孔徑的觀點,較佳係設為0.5~20莫耳%、更佳係1~10莫耳%。當使用DA-1時,DA-1使用量就從同樣的觀點,較佳係設為0.5~20莫耳%、更佳係1~10莫耳%。上述「莫耳%」係指依照下式計算出的值。 Specifically, the above-mentioned copolymerized PAA solution may be a tetrahydroxy acid dianhydride (a mixture of TA-1 and TA-2, or only TA-2) and a diamine (DA-1 and DA-) which are monomers. A mixture of 2, or only DA-2) is a solution obtained by subjecting a polymerization reaction at a temperature of 10 to 70 ° C in the above mixed solvent according to about a molar blend. Here, when TA-1 is used, the amount of TA-1 used is preferably from 0.5 to 20 mol%, more preferably from 1 to 10 mol, from the viewpoint of a higher porosity and a smaller average pore diameter. ear%. When DA-1 is used, the amount of DA-1 used is preferably from 0.5 to 20 mol%, more preferably from 1 to 10 mol%, from the same viewpoint. The above "% by mole" means a value calculated according to the following formula.

[數式2]「TA-1使用量」(莫耳%)=[「TA-1莫耳數」/(「TA-1莫耳數」+「TA-2莫耳數」)]×100「DA-1使用量」(莫耳%)=〔「DA-1莫耳數」/(「DA-1莫耳數」+「DA-2莫耳數」)]×100 [Equation 2] "TA-1 usage" (% by mole) = ["TA-1 mole number" / ("TA-1 mole number" + "TA-2 mole number")] × 100 "DA-1 Usage" (Mor%) = ["DA-1 Moir" / ("DA-1 Moir" + "DA-2 Moir")] × 100

此處,TA-1的具體例係可例如:乙二醇雙(偏苯三酸酐)(ethylene glycol bis(anhydro-trimellitate)、二乙二醇雙(偏苯三酸酐)、三乙二醇雙(偏苯三酸酐)、四乙二醇雙(偏苯三酸酐)、聚乙二醇雙(偏苯三酸酐)、乙二醇雙(偏苯三酸酐)醯胺、二乙二醇雙(偏苯三酸酐)醯胺、三乙二醇雙(偏苯三酸酐)醯胺、四乙二醇雙(偏苯三酸酐)醯胺、聚乙二醇雙(偏苯三酸酐)醯胺、丙二醇雙(偏苯三酸酐)、二丙二醇雙(偏苯三酸酐)、三丙二醇雙(偏苯三酸酐)、四丙二醇雙(偏苯三酸酐)、聚丙二醇雙(偏苯三酸酐)、丙二醇雙(偏苯三酸酐)醯胺、二丙二醇雙(偏苯三酸酐)醯胺、三丙二醇雙(偏苯三酸酐)醯胺、四丙二醇雙(偏苯三酸酐)醯胺、聚丙二醇雙(偏苯三酸酐)醯胺等。該等係可單獨使用、亦可組合使用2種以上。該等之中,較佳係聚乙二醇雙(偏苯三酸酐)醯胺、聚丙二醇雙(偏苯三酸酐)醯胺。 Here, a specific example of TA-1 may be, for example, ethylene glycol bis(trimellitic anhydride) (ethylene) Glycol bis(anhydro-trimellitate), diethylene glycol bis(trimellitic anhydride), triethylene glycol bis(trimellitic anhydride), tetraethylene glycol bis(trimellitic anhydride), polyethylene glycol bis(trimellitic anhydride), ethylene glycol bis(trimellitic anhydride)醯amine, diethylene glycol bis(trimellitic anhydride) decylamine, triethylene glycol bis(trimellitic anhydride) decylamine, tetraethylene glycol bis(trimellitic anhydride) decylamine, polyethylene glycol bis(trimellitic anhydride) decylamine, propylene glycol double (trimellitic anhydride), dipropylene glycol bis(trimellitic anhydride), tripropylene glycol bis(trimellitic anhydride), tetrapropylene glycol bis(trimellitic anhydride), polypropylene glycol bis(trimellitic anhydride), propylene glycol bis(trimellitic anhydride) decylamine, dipropylene glycol bis(trimellitic anhydride) decylamine, three Propylene glycol bis(trimellitic anhydride) decylamine, tetrapropylene glycol bis(trimellitic anhydride) decylamine, polypropylene glycol bis(trimellitic anhydride) decylamine, and the like. These may be used alone or in combination of two or more. Among these, polyethylene glycol bis(trimellitic anhydride) decylamine and polypropylene glycol bis(trimellitic anhydride) decylamine are preferred.

TA-2的具體例係可例如:均苯四甲酸二酐(PMDA)、3,3',4,4'-聯苯基四羥酸二酐(BPDA)、2,3,3',4'-聯苯基四羥酸二酐、3,3',4,4'-二苯基酮四羥酸二酐、4,4'-氧基二酞酸酐、及3,3',4,4'-二苯碸四羥酸二酐等。該等係可單獨使用、亦可組合使用2種以上。該等之中,較佳係PMDA及BPDA。 Specific examples of TA-2 can be, for example, pyromellitic dianhydride (PMDA), 3,3',4,4'-biphenyltetrahydroxy dianhydride (BPDA), 2,3,3',4 '-biphenyltetrahydroxy dianhydride, 3,3',4,4'-diphenyl ketone tetrahydroxy dianhydride, 4,4'-oxydicarboxylic anhydride, and 3,3',4, 4'-diphenylfluorene tetrahydroxy acid dianhydride and the like. These may be used alone or in combination of two or more. Among these, PMDA and BPDA are preferred.

DA-1的具體例係可例如:乙二醇雙(2-胺基乙基)醚、二乙二醇雙(2-胺基乙基)醚、三乙二醇雙(2-胺基乙基)醚、四乙二醇雙(2-胺基乙基)醚、聚乙二醇雙(2-胺基乙基)醚(PEGME)、丙二醇雙(2-胺基乙基)醚、二丙二醇雙(2-胺基乙基)醚、三丙二醇雙(2-胺基乙基)醚、四丙二醇雙(2-胺基乙基)醚、聚丙二醇雙(2-胺基乙基)醚(PPGME)、聚四氫呋喃二對胺基苯甲酸酯(PTMDA)等。該等係可單獨使用、亦 可組合使用2種以上。該等之中,較佳係PEGME、PPGME、PTMDA。PEGME、PPGM、PTGMA的數量平均分子量較佳係200~5000、更佳係500~4000。藉由將數量平均分子量設定在此種範圍內,便可更輕易地獲得具有所需平均氣孔徑的PI被膜。DA-1係可使用市售物。特別係PEGME、PPGME、PTMDA可取得例如:Jeffamine D2000(Huntsman公司製)、Jeffamine D4000(Huntsman公司製)、ELASMER-1000(IHARA CHEMICAL公司製)等。 Specific examples of DA-1 may be, for example, ethylene glycol bis(2-aminoethyl)ether, diethylene glycol bis(2-aminoethyl)ether, triethylene glycol bis(2-aminoethyl) Ether, tetraethylene glycol bis(2-aminoethyl)ether, polyethylene glycol bis(2-aminoethyl)ether (PEGME), propylene glycol bis(2-aminoethyl)ether, two Propylene glycol bis(2-aminoethyl)ether, tripropylene glycol bis(2-aminoethyl)ether, tetrapropylene glycol bis(2-aminoethyl)ether, polypropylene glycol bis(2-aminoethyl)ether (PPGME), polytetrahydrofuran di-p-aminobenzoate (PTMDA), and the like. These systems can be used separately, Two or more types can be used in combination. Among these, PEGME, PPGME, and PTMDA are preferred. The number average molecular weight of PEGME, PPGM, and PTGMA is preferably from 200 to 5,000, more preferably from 500 to 4,000. By setting the number average molecular weight within such a range, a PI film having a desired average pore diameter can be obtained more easily. Commercially available materials can be used for the DA-1 system. In particular, PEGME, PPGME, and PTMDA can be obtained, for example, Jeffamine D2000 (manufactured by Huntsman Co., Ltd.), Jeffamine D4000 (manufactured by Huntsman Co., Ltd.), and ELASMER-1000 (manufactured by IHARA CHEMICAL Co., Ltd.).

DA-2的具體例係可例如:4,4'-二胺基二苯醚(DADE)、2,2-雙[4-(4-胺基苯氧基)苯基]丙烷(BAPP)、對伸苯二胺、間伸苯二胺、2,4-二胺基甲苯、4,4'-二胺基聯苯、4,4'-二胺基-2,2'-雙(三氟甲基)聯苯、3,3'-二胺基二苯碸、4,4'-二胺基二苯碸、4,4'-二胺基二苯硫醚、4,4'-二胺基二苯甲烷、3,4'-二胺基二苯醚、3,3'-二胺基二苯醚、1,4-雙(4-胺基苯氧基)苯、1,3-雙(4-胺基苯氧基)苯、1,3-雙(3-胺基苯氧基)苯、4,4'-雙(4-胺基苯氧基)聯苯、雙[4-(4-胺基苯氧基)苯基]碸、雙[4-(3-胺基苯氧基)苯基]碸、2,2-雙[4-(4-胺基苯氧基)苯基]六氟丙烷、α,ω-雙胺基聚二甲基矽氧烷、α,ω-雙(3-胺基丙基)聚二甲基矽氧烷、1,3-雙(3-胺基丙基)四甲基二矽氧烷、1,3-雙(3-胺基丙基)-1,1,3,3-四甲基二矽氧烷、雙(10-胺基十亞甲基)四甲基二矽氧烷、雙(3-胺基苯氧基甲基)四甲基二矽氧烷、α,ω-雙(3-胺基丙基)聚甲基苯基矽氧烷、α,ω-雙(3-胺基丙基)聚(二甲基矽氧烷-二苯基矽氧烷)共聚物等。該等係可單獨使用、亦可組合使用2種以上。該等之中,較佳係DADE、BAPP。 Specific examples of DA-2 may be, for example, 4,4'-diaminodiphenyl ether (DADE), 2,2-bis[4-(4-aminophenoxy)phenyl]propane (BAPP), P-phenylenediamine, m-phenylenediamine, 2,4-diaminotoluene, 4,4'-diaminobiphenyl, 4,4'-diamino-2,2'-bis(trifluoro Methyl)biphenyl, 3,3'-diaminodiphenyl hydrazine, 4,4'-diaminodiphenyl hydrazine, 4,4'-diaminodiphenyl sulfide, 4,4'-diamine Diphenylmethane, 3,4'-diaminodiphenyl ether, 3,3'-diaminodiphenyl ether, 1,4-bis(4-aminophenoxy)benzene, 1,3-double (4-Aminophenoxy)benzene, 1,3-bis(3-aminophenoxy)benzene, 4,4'-bis(4-aminophenoxy)biphenyl, bis[4-( 4-aminophenoxy)phenyl]anthracene, bis[4-(3-aminophenoxy)phenyl]anthracene, 2,2-bis[4-(4-aminophenoxy)phenyl Hexafluoropropane, α,ω-diaminopolydimethyloxane, α,ω-bis(3-aminopropyl)polydimethyloxane, 1,3-bis(3-amine Propyl)tetramethyldioxane, 1,3-bis(3-aminopropyl)-1,1,3,3-tetramethyldioxane, bis(10-amino-based Methyl)tetramethyldioxane, bis(3-aminophenoxymethyl)tetramethyldioxane, α,ω-bis(3-aminopropyl)polymethylphenylhydrazine Alkyl, α, ω- bis (3-aminopropyl) poly (dimethyl siloxane Silicon - Silicon diphenyl siloxane) copolymers. These may be used alone or in combination of two or more. Among these, DADE and BAPP are preferred.

共聚合PAA溶液係利用例如:在良溶劑中進行聚合反應而獲得溶液後,再於其中添加不良溶劑的方法,以及在不良溶劑中進行聚合反應而獲得懸浮液後,再於其中添加良溶劑的方法亦可獲得。 The copolymerized PAA solution is obtained by, for example, a method of obtaining a solution by carrying out a polymerization reaction in a good solvent, adding a poor solvent thereto, and performing a polymerization reaction in a poor solvent to obtain a suspension, and then adding a good solvent thereto. The method is also available.

在共聚合PAA溶液中,視需要於不致損及本發明效果之範圍內,亦可添加各種界面活性劑及/或矽烷偶合劑之類的公知添加物。又,視需要在不致損及本發明效果之範圍內,亦可在共聚合PAA溶液中添加PI以外的其他高分子。 In the copolymerized PAA solution, a known additive such as various surfactants and/or a decane coupling agent may be added as needed within the range which does not impair the effects of the present invention. Further, a polymer other than PI may be added to the copolymerized PAA solution as needed within the range which does not impair the effects of the present invention.

將共聚合PAA溶液塗佈於基材表面,經乾燥便可形成多孔質PI薄膜。然後,從基材上剝離多孔質PI薄膜便可成為多孔質PI薄膜單體。又,在基材上所形成的多孔質PI薄膜亦可不從基材上剝離,而與基材呈積層一體化使用。 The copolymerized PAA solution is applied to the surface of the substrate and dried to form a porous PI film. Then, the porous PI film is peeled off from the substrate to form a porous PI film monomer. Further, the porous PI film formed on the substrate may be used in combination with the substrate without being peeled off from the substrate.

上述乾燥步驟係包括有:藉由使塗膜中所含的溶劑揮發,而誘發相分離使多孔質PAA被膜形成的步驟1;以及將上述多孔質PAA被膜施行熱醯亞胺化,而成為多孔質PI被膜的步驟2。步驟1的溫度較佳係100~200℃左右,步驟2的溫度係未滿350℃的溫度,例如較佳依300℃實施。若步驟2時的溫度設為350℃以上,便會有導致被導入至PI中的氧化伸烷基單元其中一部分發生熱分解的虞慮。 The drying step includes a step 1 of inducing phase separation to form a porous PAA film by volatilizing a solvent contained in the coating film, and a heat-imidization of the porous PAA film to become porous Step 2 of the PI coating. The temperature of the step 1 is preferably about 100 to 200 ° C, and the temperature of the step 2 is less than 350 ° C, for example, preferably 300 ° C. When the temperature at the step 2 is set to 350 ° C or higher, there is a concern that a part of the alkylene oxide unit introduced into the PI is thermally decomposed.

上述基材係可例如:金屬箔、金屬線、玻璃板、塑膠薄膜、各種織物、各種不織布等,上述金屬係可使用金、銀、銅、鉑、鋁等。 該等係可為多孔質、亦可為非多孔質。塗液對該基材的塗佈方法係可使用浸塗機、棒塗機、旋塗機、模具塗佈機、噴霧塗佈機等,依連續式或批次式施行塗佈。 The substrate may be, for example, a metal foil, a metal wire, a glass plate, a plastic film, various woven fabrics, or various nonwoven fabrics, and the metal may be made of gold, silver, copper, platinum, aluminum or the like. These systems may be porous or non-porous. The coating method of the coating liquid can be applied in a continuous or batch manner using a dip coater, a bar coater, a spin coater, a die coater, a spray coater or the like.

具有連續氣孔的本發明之多孔質PI薄膜,係可在其表面(單面或雙面)上形成活性層。藉此可將本發明的多孔質PI薄膜使用為逆滲透膜或氣體分離膜。此處所謂「活性層」係指由具有分離功能的有機高分子及/或無機化合物所構成非多孔質薄膜形成之層,藉由設置此種層,便可將本發明的多孔質PI薄膜使用為逆滲透膜或氣體分離膜。活性層的厚度通常係0.01~500nm左右,藉由設為此種極薄膜,便可同時確保良好的分離性能與穿透性能。因為本發明之多孔質PI薄膜的平均氣孔徑係10~1000nm的極小程度,因而可均勻形成上述極薄膜。 The porous PI film of the present invention having continuous pores can form an active layer on its surface (single or double sided). Thereby, the porous PI film of the present invention can be used as a reverse osmosis membrane or a gas separation membrane. Here, the "active layer" means a layer formed of a non-porous film composed of an organic polymer having a separation function and/or an inorganic compound, and by providing such a layer, the porous PI film of the present invention can be used. It is a reverse osmosis membrane or a gas separation membrane. The thickness of the active layer is usually about 0.01 to 500 nm, and by using such an electrode film, good separation performance and penetration performance can be ensured at the same time. Since the average pore diameter of the porous PI film of the present invention is extremely small from 10 to 1000 nm, the above-mentioned electrode film can be uniformly formed.

將本發明之多孔質PI薄膜使用為逆滲透膜時,例如只要在上述多孔質PI被膜的表面(單面或雙面)上,形成由芳醯胺等構成的活性層便可。在形成該等活性層時,可採用例如日本專利特公平7-90152號公報及日本專利第3181134號公報所揭示的公知方法。 When the porous PI film of the present invention is used as a reverse osmosis membrane, for example, an active layer composed of linaloamine or the like may be formed on the surface (single or both surfaces) of the porous PI film. In the case of forming such an active layer, a known method disclosed in, for example, Japanese Patent Publication No. Hei 7-90152 and Japanese Patent No. 3181134 can be employed.

再者,當將本發明的多孔質PI薄膜使用為氣體分離膜(例如氫氣分離膜)時,例如只要使由鈀、鈀/銀合金、鈀/銅合金等極薄膜構成的活性層,形成於上述多孔質PI被膜的表面(單面或雙面)上便可。在形成該等活性層時,可採用例如:Journal of Membrane Science Volume 94,Issue 1,19 September 1994,Pages 299-311、及美國專利 4857080號所揭示的公知方法。 In addition, when the porous PI film of the present invention is used as a gas separation membrane (for example, a hydrogen separation membrane), for example, an active layer composed of an epipolar thin film such as palladium, palladium/silver alloy or palladium/copper alloy is formed. The surface of the porous PI film (single or double sided) may be used. In forming such active layers, for example, Journal of Membrane Science Volume 94, Issue 1, 19 September 1994, Pages 299-311, and US patents may be employed. A known method disclosed in No. 4,857,080.

本發明之多孔質PI薄膜的厚度通常係1~1000μm左右,較佳係10~500μm左右。 The thickness of the porous PI film of the present invention is usually about 1 to 1000 μm, preferably about 10 to 500 μm.

上述氣孔率及平均氣孔徑係藉由選擇共聚合PAA溶液中的溶劑(良溶劑及不良溶劑)種類及/或調配量,便可調整。 The porosity and the average pore diameter can be adjusted by selecting the type and/or the amount of the solvent (good solvent and poor solvent) in the copolymerized PAA solution.

如上述,因為本發明的製法並未使用造孔劑,因而可獲得實質不會殘留造孔劑的本發明之多孔質PI薄膜。 As described above, since the pore-forming agent is not used in the production method of the present invention, the porous PI film of the present invention which does not substantially remain as a pore-forming agent can be obtained.

[實施例] [Examples]

以下,舉實施例,針對本發明進行更詳細說明。另外,本發明並不因實施例而受限定。 Hereinafter, the present invention will be described in more detail by way of examples. In addition, the invention is not limited by the examples.

〔實施例1〕 [Example 1]

在玻璃製反應容器中,於氮環境下,投入DADE(DA-2):0.94莫耳、PPGME(DA-1):0.06莫耳(分子量2000:Huntsman公司製Jeffamine D2000)、以及由DMAc與四乙二醇二甲醚構成的混合溶劑(DMAc/四乙二醇二甲醚混合比率依質量比計為25/75),並攪拌、溶解二胺成分。該溶液一邊利用夾套冷卻至30℃以下,一邊徐緩投入PMDA(TA-2):1.03莫耳後,於40℃進行5小時聚合反應,獲得經導入氧化伸丙基單元的共聚合PAA溶液。該溶液的固形份濃度係21質量%。將上述共聚合PAA溶液使用刮漿刀塗佈於鋁箔(厚 度:150μm)上,依130℃乾燥20分鐘,獲得由共聚合PAA構成的塗膜。接著,在氮氣流中,歷時120分鐘升溫至300℃,依300℃施行追加乾燥60分鐘,而將共聚合PAA施行醯亞胺化,獲得在鋁箔上積層厚度約30μm的多孔質PI薄膜(P-1)。P-1的截面與表面之SEM影像,如圖1及圖2所示。 In a glass reaction vessel, DADE (DA-2) was charged under a nitrogen atmosphere: 0.94 mol, PPGME (DA-1): 0.06 mol (molecular weight: 2000: Jeffamine D2000 manufactured by Huntsman Co., Ltd.), and DMAc and four. A mixed solvent of ethylene glycol dimethyl ether (the ratio of DMAc/tetraethylene glycol dimethyl ether is 25/75 by mass ratio), and the diamine component is stirred and dissolved. This solution was cooled to 30 ° C or less by a jacket, and was slowly introduced into PMDA (TA-2): 1.03 mol, and then subjected to a polymerization reaction at 40 ° C for 5 hours to obtain a copolymerized PAA solution introduced into an oxypropyl unit. The solid concentration of the solution was 21% by mass. Applying the above copolymerized PAA solution to aluminum foil using a doctor blade (thick On a 150 μm basis, it was dried at 130 ° C for 20 minutes to obtain a coating film composed of copolymerized PAA. Subsequently, the temperature was raised to 300 ° C in a nitrogen stream for 120 minutes, and additional drying was carried out at 300 ° C for 60 minutes, and the copolymerized PAA was imidized to obtain a porous PI film having a thickness of about 30 μm on the aluminum foil. -1). The SEM image of the cross section and surface of P-1 is shown in Figures 1 and 2.

多孔質PI薄膜(P-1)的氣孔率、平均氣孔徑係如表-1所示。又,表面的開口率、平均開口徑分別係52%、650nm。又,所獲得積層體以200℃及250℃施行1小時熱處理,經測定多孔質PI薄膜(P-1)表面的電阻值後,結果電阻值幾乎與處理前沒有變化,確認到良好耐熱性。 The porosity and average pore diameter of the porous PI film (P-1) are shown in Table-1. Further, the aperture ratio and the average opening diameter of the surface were 52% and 650 nm, respectively. In addition, the obtained laminate was heat-treated at 200 ° C and 250 ° C for 1 hour, and the resistance value of the surface of the porous PI film (P-1) was measured. As a result, the resistance value was almost unchanged from that before the treatment, and good heat resistance was confirmed.

〔實施例2〕 [Example 2]

除使用DMAc/四乙二醇二甲醚的混合比率依質量比設為15/85的混合溶劑之外,其餘均與實施例1同樣地製成共聚合PAA溶液,並與實施例1同樣地獲得在鋁箔上積層厚度約25μm的多孔質PI薄膜(P-2)。P-2的氣孔率、平均氣孔徑係如表-1所示。 A copolymerized PAA solution was prepared in the same manner as in Example 1 except that the mixing ratio of DMAc/tetraethylene glycol dimethyl ether was changed to 15/85 by mass ratio, and the same procedure as in Example 1 was carried out. A porous PI film (P-2) having a thickness of about 25 μm laminated on the aluminum foil was obtained. The porosity and average pore diameter of P-2 are shown in Table-1.

〔實施例3〕 [Example 3]

除DA-1係使用PPGME(Huntsman公司製Jeffamine D4000、分子量:4000)0.03莫耳,且DA-2係使用DADE:0.97莫耳用之外,其餘均與實施例1同樣地製成共聚合PAA溶液,並與實施例1同樣地獲得在鋁箔上積層厚度約30μm的多孔質PI薄膜(P-3)。多孔質PI薄膜(P-3)的氣孔率、平均氣孔徑係如表-1所示。 A copolymerized PAA was prepared in the same manner as in Example 1 except that DA-1 was used in which PPGME (Jeffamine D4000 manufactured by Huntsman Co., Ltd., molecular weight: 4000) was 0.03 mol, and DA-2 was used as DADE: 0.97 mol. In the same manner as in Example 1, a porous PI film (P-3) having a thickness of about 30 μm laminated on the aluminum foil was obtained in the same manner as in Example 1. The porosity and average pore diameter of the porous PI film (P-3) are shown in Table-1.

〔實施例4〕 [Example 4]

除DA-1係使用PTMDA:0.06莫耳(分子量1000:IHARA CHEMICAL公司製ELASMER-1000)之外,其餘均與實施例1同樣地製成共聚合PAA溶液,並與實施例1同樣地獲得在鋁箔上積層厚度約30μm的多孔質PI薄膜(P-4)。多孔質PI薄膜(P-4)的氣孔率、平均氣孔徑係如表-1所示。 A copolymerized PAA solution was prepared in the same manner as in Example 1 except that DATM was used in the same manner as in Example 1 except that PTMDA: 0.06 mol (molecular weight: ELASMER-1000 manufactured by IHARA CHEMICAL Co., Ltd.) was used. A porous PI film (P-4) having a thickness of about 30 μm was laminated on the aluminum foil. The porosity and average pore diameter of the porous PI film (P-4) are shown in Table-1.

〔實施例5〕 [Example 5]

除TA-2係使用BPDA:1.03莫耳之外,其餘均與實施例1同樣地製成共聚合PAA溶液,並與實施例1同樣地獲得在鋁箔上積層厚度約30μm的多孔質PI薄膜(P-5)。多孔質PI薄膜(P-5)的氣孔率、平均氣孔徑係如表-1所示。 A porous PI film having a thickness of about 30 μm laminated on an aluminum foil was obtained in the same manner as in Example 1 except that the TA-2 system was used in the same manner as in Example 1 except that BPDA: 1.03 mole was used. P-5). The porosity and average pore diameter of the porous PI film (P-5) are shown in Table-1.

〔實施例6〕 [Example 6]

除TA-2係使用BPDA:1.03莫耳,且將DMAc/四乙二醇二甲醚的混合比率依質量比計設為35/65之外,其餘均與實施例1同樣地製成共聚合PAA溶液,獲得在鋁箔上積層厚度約35μm的多孔質PI薄膜(P-6)。多孔質PI薄膜(P-6)的氣孔率、平均氣孔徑係如表-1所示。 Copolymerization was carried out in the same manner as in Example 1 except that the TA-2 system used BPDA: 1.03 mol, and the mixing ratio of DMAc/tetraethylene glycol dimethyl ether was 35/65 by mass ratio. As the PAA solution, a porous PI film (P-6) having a thickness of about 35 μm laminated on the aluminum foil was obtained. The porosity and average pore diameter of the porous PI film (P-6) are shown in Table-1.

〔實施例7〕 [Example 7]

除醚系溶劑係使用由四乙二醇二甲醚50質量份與三乙二醇二甲醚50質量份構成的混合溶劑之外,其餘均與實施例1同樣地製 成共聚合PAA溶液,獲得在鋁箔上積層厚度約30μm的多孔質PI薄膜(P-7)。P-7的氣孔率、平均氣孔徑係如表-1所示。 The same procedure as in Example 1 was carried out except that the ether solvent was a mixed solvent of 50 parts by mass of tetraethylene glycol dimethyl ether and 50 parts by mass of triethylene glycol dimethyl ether. The PAA solution was co-polymerized to obtain a porous PI film (P-7) having a thickness of about 30 μm laminated on the aluminum foil. The porosity and average pore diameter of P-7 are shown in Table-1.

〔實施例8〕 [Example 8]

除DA-2係使用由DADE:0.8莫耳與BAPP:0.14莫耳構成的混合物之外,其餘均與實施例1同樣地製成共聚合PAA溶液,獲得在鋁箔上積層厚度約30μm的多孔質PI薄膜(P-8)。P-8的氣孔率、平均氣孔徑係如表-1所示。 A copolymerized PAA solution was prepared in the same manner as in Example 1 except that the DA-2 system was a mixture of DADE: 0.8 mol and BAPP: 0.14 mol, and a porous layer having a thickness of about 30 μm on the aluminum foil was obtained. PI film (P-8). The porosity and average pore diameter of P-8 are shown in Table-1.

〔實施例9〕 [Example 9]

將實施例1所獲得共聚合PAA溶液,使用刮漿刀塗佈於聚酯薄膜(厚度:200μm)上,於130℃乾燥20分鐘,獲得由共聚合PAA構成的塗膜。接著,將該塗膜從聚酯薄膜上剝離,接著在氮氣流中,歷時120分鐘升溫至250℃,於250℃施行追加乾燥60分鐘,而將共聚合PAA施行醯亞胺化,獲得厚度約50μm的多孔質PI薄膜(P-9)。P-9的氣孔率、平均氣孔徑係如表-1所示。P-9於200℃施行1小時處理,經測定尺寸變化率,結果在1%以下,確認到良好的耐熱性。 The copolymerized PAA solution obtained in Example 1 was applied onto a polyester film (thickness: 200 μm) using a doctor blade, and dried at 130 ° C for 20 minutes to obtain a coating film composed of copolymerized PAA. Next, the coating film was peeled off from the polyester film, and then heated to 250 ° C in a nitrogen stream for 120 minutes, and additionally dried at 250 ° C for 60 minutes, and the copolymerized PAA was imidized to obtain a thickness of about 5%. 50 μm porous PI film (P-9). The porosity and average pore diameter of P-9 are shown in Table-1. P-9 was treated at 200 ° C for 1 hour, and the dimensional change rate was measured, and as a result, it was 1% or less, and good heat resistance was confirmed.

<比較例1> <Comparative Example 1>

除單體係使用DADE(DA-2):1莫耳、PMDA(TA-2):1.03莫耳之外,其餘均與實施例1同樣地製成PAA溶液,並與實施例1同樣地獲得在鋁箔上積層厚度約30μm的多孔質PI薄膜(R-1)。多孔質PI薄膜(R-1)截面的SEM影像係如圖3所示。多孔質PI薄膜(R-1) 的氣孔率、平均氣孔徑係如表-1所示。 A PAA solution was prepared in the same manner as in Example 1 except that DADE (DA-2): 1 mol, PMDA (TA-2): 1.03 mol was used, and the same procedure as in Example 1 was obtained. A porous PI film (R-1) having a thickness of about 30 μm was laminated on the aluminum foil. The SEM image of the cross section of the porous PI film (R-1) is shown in Fig. 3. Porous PI film (R-1) The porosity and average pore size are shown in Table-1.

<比較例2> <Comparative Example 2>

除使用DMAc/四乙二醇二甲醚的混合比率依質量比計設為60/40的混合溶劑之外,其餘均與實施例1同樣地製成PAA溶液,並與實施例1同樣地獲得在鋁箔上積層厚度約30μm的多孔質PI薄膜(R-2)。多孔質PI薄膜(R-2)的氣孔率、平均氣孔徑係如表-1所示。 A PAA solution was prepared in the same manner as in Example 1 except that the mixing ratio of DMAc/tetraethylene glycol dimethyl ether was 60/40 by mass ratio, and the same procedure as in Example 1 was obtained. A porous PI film (R-2) having a thickness of about 30 μm was laminated on the aluminum foil. The porosity and average pore diameter of the porous PI film (R-2) are shown in Table-1.

<比較例3> <Comparative Example 3>

除使用DMAc/四乙二醇二甲醚的混合比率依質量比計設為50/50的混合溶劑之外,其餘均與實施例1同樣地製成PAA溶液,並與實施例1同樣地獲得在鋁箔上積層厚度約30μm的多孔質PI薄膜(R-3)。多孔質PI薄膜(R-3)的氣孔率、平均氣孔徑係如表-1所示。 A PAA solution was prepared in the same manner as in Example 1 except that the mixing ratio of DMAc/tetraethylene glycol dimethyl ether was 50/50 by mass ratio, and the same procedure as in Example 1 was obtained. A porous PI film (R-3) having a thickness of about 30 μm was laminated on the aluminum foil. The porosity and average pore diameter of the porous PI film (R-3) are shown in Table-1.

如實施例所示,得知本發明的多孔質PI薄膜P-1~P-9,均勻地形成氣孔率達45體積%以上、平均氣孔徑在1000nm以下的微細氣孔。相對於此,得知比較例的多孔質PI薄膜R-1並沒有形成平均氣孔徑在1000nm以下的微細氣孔。又,得知比較例的多孔質PI薄膜R-2、R-3並無法獲得高氣孔率。 As shown in the examples, it was found that the porous PI films P-1 to P-9 of the present invention uniformly formed fine pores having a porosity of 45% by volume or more and an average pore diameter of 1000 nm or less. On the other hand, it was found that the porous PI thin film R-1 of the comparative example did not form fine pores having an average pore diameter of 1000 nm or less. Further, it was found that the porous PI films R-2 and R-3 of the comparative examples were not able to obtain a high porosity.

(產業上之可利用性) (industrial availability)

形成有多數微細氣孔的本發明多孔質PI薄膜,因為並沒有使用造孔劑等氣孔形成劑,因而不會有該等殘留的情形。所以,作為耐熱性多孔質薄膜,可使用於例如:低介電常數基板等電子材料、鋰二次電池用隔板、燃料電池的固體電解質負載膜、過濾器、分離膜、電線被覆等產業用材料、醫療材料、光學材料的素材等。 The porous PI film of the present invention in which a large number of fine pores are formed does not have such a residual state because a pore forming agent such as a pore former is not used. Therefore, the heat-resistant porous film can be used for, for example, an electronic material such as a low dielectric constant substrate, a separator for a lithium secondary battery, a solid electrolyte supporting film for a fuel cell, a filter, a separation membrane, and a wire coating. Materials, medical materials, materials for optical materials, etc.

Claims (3)

一種多孔質聚醯亞胺薄膜,其特徵在於,由含氧化伸烷基單元的聚醯亞胺構成,氣孔率係45體積%以上且95體積%以下,平均氣孔徑係10nm以上且1000nm以下。 A porous polyimine film comprising a polyamidene containing an alkylene oxide unit, having a porosity of 45 vol% or more and 95 vol% or less, and an average pore diameter of 10 nm or more and 1000 nm or less. 如請求項1之多孔質聚醯亞胺薄膜,其中,在表面上形成活性層。 A porous polyimide film according to claim 1, wherein an active layer is formed on the surface. 一種請求項1或2之多孔質聚醯亞胺薄膜之製造方法,其特徵在於,將由含氧化伸烷基單元之聚醯胺酸、與含其良溶劑與不良溶劑的混合溶劑構成,且上述混合溶劑中的不良溶劑比率係65質量%以上且95質量%以下的溶液,塗佈於基材上之後,依未滿350℃的溫度施行乾燥。 A method for producing a porous polyimine film according to claim 1 or 2, which comprises a polyphthalic acid containing an alkylene oxide unit and a mixed solvent containing a good solvent and a poor solvent, and the above The solution having a poor solvent ratio in the mixed solvent of 65 mass% or more and 95 mass% or less is applied to the substrate, and then dried at a temperature of less than 350 °C.
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