TW202206497A - A fluorine-containing dispersion and its preparation method, a fluorine-containing composite membrane and its application - Google Patents
A fluorine-containing dispersion and its preparation method, a fluorine-containing composite membrane and its application Download PDFInfo
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本發明涉及高分子薄膜製備的技術領域,尤其涉及一種含氟分散液的製備方法、含氟復合膜及其應用。The invention relates to the technical field of polymer film preparation, in particular to a preparation method of a fluorine-containing dispersion liquid, a fluorine-containing composite membrane and applications thereof.
傳統的離型膜或離型紙不耐高溫,於高溫環境下會產生收縮及離型能力失效等情況,因此,無法適用於高溫製程或含有高沸點溶劑的塗布成膜製程,例如聚醯亞胺薄膜的製備過程就無法使用傳統的離型膜或離型紙。The traditional release film or release paper is not resistant to high temperature, and will shrink and lose its release ability under high temperature environment. Therefore, it is not suitable for high temperature process or coating film formation process containing high boiling point solvents, such as polyimide The production process of the film cannot use the traditional release film or release paper.
目前,聚醯亞胺薄膜的製備需要採用鋼帶進行塗布作業,具體方法包括:將聚醯胺酸溶液塗布於鋼帶上並進行烘烤,可得到聚醯胺酸薄膜卷料,再將其於高溫環化爐進行熟化,兩側使用夾具固定聚醯胺酸薄膜,同時進行橫向(TD)和縱向(MD)延伸。在拉伸過程中,需要控制的關鍵參數包括聚醯胺酸薄膜的張力大小、機械強度、厚度、熟化所產生的收縮力以及需要保證縱向(MD)及橫向(TD)機械強度差異不能太大,造成聚醯亞胺薄膜的製程限制門檻高。同時傳統的拉伸製程不適用熱塑性的聚醯亞胺配方,原因是在高溫時聚醯胺酸薄膜會出現薄膜塌陷現象及沾黏夾具的情形,因此傳統的聚醯亞胺薄膜的製備方法限制了聚醯胺酸溶液配方的選擇。At present, the preparation of the polyimide film requires the use of a steel strip for coating operations. The specific method includes: coating the polyimide solution on the steel strip and baking it to obtain a polyimide film roll, and then applying the It is aged in a high temperature cyclization furnace, and the polyamide film is fixed with clamps on both sides, and the transverse (TD) and longitudinal (MD) stretches are carried out at the same time. During the stretching process, the key parameters that need to be controlled include the tensile strength, mechanical strength, thickness, shrinkage force generated by aging and the need to ensure that the difference between the longitudinal (MD) and transverse (TD) mechanical strengths of the polyamide film is not too large. , resulting in a high process limit threshold for polyimide films. At the same time, the traditional stretching process is not suitable for thermoplastic polyimide formulations, because the polyimide film will collapse and stick to the fixture at high temperature. Therefore, the preparation method of traditional polyimide film is limited. The choice of polyamide solution formulation was discussed.
為了解決上述技術問題,本發明提出一種含氟分散液及其製備方法、含氟復合膜及其應用,該含氟復合膜採用含氟分散液製備而成,該含氟復合膜用於製備聚醯亞胺薄膜或聚酯薄膜等高分子薄膜,本發明實施方式以採用含氟復合膜製備聚醯亞胺薄膜為例進行說明。In order to solve the above-mentioned technical problems, the present invention proposes a fluorine-containing dispersion liquid and a preparation method thereof, a fluorine-containing composite film and an application thereof. For polymer films such as imide films or polyester films, the embodiments of the present invention will be described by taking a fluorine-containing composite film to prepare a polyimide film as an example.
本發明提供一種含氟分散液,所述含氟分散液的固成分包括含氟高分子粉體和聚醯亞胺,所述含氟高分子粉體的粒徑小於或等於3μm,所述含氟高分子粉體在所述含氟分散液的固成分中的重量百分比大於或等於85%,所述聚醯亞胺在所述含氟分散液的固成分中的重量百分比小於或等於15%。The present invention provides a fluorine-containing dispersion liquid. The solid content of the fluorine-containing dispersion liquid includes a fluorine-containing polymer powder and a polyimide. The particle size of the fluorine-containing polymer powder is less than or equal to 3 μm. The weight percentage of the fluorine polymer powder in the solid content of the fluorine-containing dispersion is greater than or equal to 85%, and the weight percentage of the polyimide in the solid content of the fluorine-containing dispersion is less than or equal to 15% .
進一步,所述含氟分散液的固含量為40wt%~50 wt%。Further, the solid content of the fluorine-containing dispersion liquid is 40 wt % to 50 wt %.
進一步,所述含氟高分子粉體包括聚四氟乙烯、全氟烷氧基、聚全氟乙丙烯、三氟氯乙烯、乙烯-三氟氯乙烯及聚全氟亞乙烯基中的一種或幾種。Further, the fluorine-containing polymer powder includes one or more of polytetrafluoroethylene, perfluoroalkoxy, polyperfluoroethylene propylene, trifluorochloroethylene, ethylene-trifluorochloroethylene and polyperfluoroethylene vinylene. several.
本發明還提供一種含氟分散液的製備方法,包括以下步驟:The present invention also provides a method for preparing a fluorine-containing dispersion, comprising the following steps:
提供第一混合液,所述第一混合液包括含氟高分子粉體,所述含氟高分子粉體的平均粒徑小於或等於3μm。A first mixed solution is provided, the first mixed solution includes fluorine-containing polymer powder, and the average particle size of the fluorine-containing polymer powder is less than or equal to 3 μm.
於所述第一混合液中加入聚醯亞胺溶液,混合得到所述含氟分散液。A polyimide solution is added to the first mixed solution, and mixed to obtain the fluorine-containing dispersion.
所述聚醯亞胺溶液包括聚醯亞胺,所述含氟高分子粉體和所述聚醯亞胺組成所述含氟分散液的固成分,所述含氟高分子粉體在所述含氟分散液的固成分中的重量百分比大於或等於85%,所述聚醯亞胺在所述含氟分散液的固成分中的重量百分比小於或等於15%。The polyimide solution includes polyimide, the fluorine-containing polymer powder and the polyimide constitute the solid content of the fluorine-containing dispersion, and the fluorine-containing polymer powder is in the The weight percentage in the solid content of the fluorine-containing dispersion is greater than or equal to 85%, and the weight percentage of the polyimide in the solid content of the fluorine-containing dispersion is less than or equal to 15%.
進一步,所述含氟分散液的固含量為40wt%~50 wt%。Further, the solid content of the fluorine-containing dispersion liquid is 40 wt % to 50 wt %.
進一步,所述含氟高分子粉體包括聚四氟乙烯、全氟烷氧基、聚全氟乙丙烯、三氟氯乙烯、乙烯-三氟氯乙烯及聚全氟亞乙烯基中的一種或幾種。Further, the fluorine-containing polymer powder includes one or more of polytetrafluoroethylene, perfluoroalkoxy, polyperfluoroethylene propylene, trifluorochloroethylene, ethylene-trifluorochloroethylene and polyperfluoroethylene vinylene. several.
本發明還提供一種含氟復合膜,包括一基材及設於所述基材至少一表面的含氟膜,所述含氟膜由如上所述的含氟分散液加熱後製得。The present invention also provides a fluorine-containing composite membrane, comprising a substrate and a fluorine-containing membrane disposed on at least one surface of the substrate, wherein the fluorine-containing membrane is prepared by heating the above-mentioned fluorine-containing dispersion.
進一步,所述基材為聚醯亞胺膜,所述基材的厚度為125μm~225μm。Further, the base material is a polyimide film, and the thickness of the base material is 125 μm˜225 μm.
進一步,所述含氟膜的厚度為3μm~6μm。Further, the thickness of the fluorine-containing film is 3 μm˜6 μm.
進一步,所述含氟復合膜包括含氟高分子粉體和聚苯惡唑,所述含氟高分子粉體在所述含氟復合膜中的重量百分比大於或等於85%,所述聚苯惡唑在所述含氟復合膜中的重量百分比小於或等於15%。Further, the fluorine-containing composite film includes fluorine-containing polymer powder and polybenzoxazole, and the weight percentage of the fluorine-containing polymer powder in the fluorine-containing composite film is greater than or equal to 85%, and the polyphenylene The weight percentage of oxazole in the fluorine-containing composite membrane is less than or equal to 15%.
本發明還提供一種含氟復合膜的製備方法,包括以下步驟:The present invention also provides a preparation method of the fluorine-containing composite membrane, comprising the following steps:
提供一基材。A substrate is provided.
於所述基材的至少一表面塗布如上所述的含氟分散液並乾燥,得到中間體。The above-mentioned fluorine-containing dispersion is coated on at least one surface of the substrate and dried to obtain an intermediate.
將所述中間體於400℃~450℃進行燒結,得到所述含氟復合膜。The intermediate body is sintered at 400° C. to 450° C. to obtain the fluorine-containing composite film.
本發明還提供一種聚合物薄膜的製備方法,包括以下步驟:The present invention also provides a preparation method of the polymer film, comprising the following steps:
提供一聚合物溶液和如上所述的含氟復合膜。A polymer solution and a fluorine-containing composite membrane as described above are provided.
於所述含氟膜遠離所述基材的表面塗布所述聚合物溶液並進行烘烤,從而形成一中間膜層。The polymer solution is coated on the surface of the fluorine-containing film away from the substrate and baked to form an intermediate film layer.
將所述中間膜層進行熟化,以形成所述聚合物薄膜。The intermediate film layer is aged to form the polymer film.
進一步,所述熟化包括以下步驟:Further, the curing comprises the following steps:
將所述中間膜層和所述含氟復合膜收卷,使得所述膜層朝外,以得到半成品膜卷材。The intermediate film layer and the fluorine-containing composite film are wound so that the film layer faces outward to obtain a semi-finished film roll.
將所述半成品膜卷材於氮氣環境下加熱進行熟化,以形成所述聚合物薄膜。The semi-finished film roll is heated and aged under a nitrogen atmosphere to form the polymer film.
將所述聚合物薄膜和所述含氟復合膜分別收卷。The polymer film and the fluorine-containing composite film are respectively wound up.
進一步,所述熟化包括以下步驟:Further, the curing comprises the following steps:
將所述中間膜層和所述含氟復合膜採用懸浮式RTR工藝於氮氣環境下加熱進行線上熟化,以形成所述聚合物薄膜。The intermediate film layer and the fluorine-containing composite film are heated in a nitrogen atmosphere by a suspended RTR process for online aging, so as to form the polymer film.
將所述聚合物薄膜和所述含氟復合膜分別收卷。The polymer film and the fluorine-containing composite film are respectively wound up.
相較於習知技術,本發明的有益效果在於:含氟復合膜中由於聚苯惡唑的存在,保有耐高溫特性,使含氟復合膜在高溫條件下依然具有離型力,適用於高溫製程或含有高沸點溶劑的塗布成膜製程;可藉由調整含氟高分子粉體和聚苯惡唑的比例,可以調整含氟復合膜的離型力大小,適用於對離型力有不同要求的多種聚合物溶液成膜,提高了聚合物溶液的配方選擇性;含氟復合膜可實現雙面離型,適用於傳統的批次成卷高溫熟化,避免成卷熟化過程中層間沾黏等問題,同時雙離型面可以同時成膜,提高了生產效率;由於含氟復合膜位於中間層的聚醯亞胺膜的厚度較厚,具有足夠的挺度和韌性,可採用含氟復合膜作為承載體直接進行塗布成膜製程,且可適用於懸浮式線上高溫熟化製程,提高生產效率,且可減少捲曲現象;可採用含氟復合膜作為承載體進行塗布成膜製程,無需橫向及縱向拉伸過程,降低了製程門檻;成膜製程中無含氧量限制,且含氟復合膜可以多次回收利用,節約成本,同時符合環保趨勢。Compared with the prior art, the beneficial effect of the present invention is: due to the existence of polybenzoxazole in the fluorine-containing composite film, high temperature resistance is maintained, so that the fluorine-containing composite film still has release force under high temperature conditions, which is suitable for high temperature. Process or coating and film-forming process containing high boiling point solvent; by adjusting the ratio of fluorine-containing polymer powder and polybenzoxazole, the release force of the fluorine-containing composite film can be adjusted, which is suitable for different release forces. Various polymer solutions are required to form films, which improves the formulation selectivity of polymer solutions; fluorine-containing composite films can realize double-sided release, which is suitable for traditional batch high-temperature curing in rolls to avoid interlayer sticking during roll curing. At the same time, the double release surface can form a film at the same time, which improves the production efficiency; because the thickness of the polyimide film with the fluorine-containing composite film in the middle layer is thick and has sufficient stiffness and toughness, the fluorine-containing composite film can be used. The film is used as a carrier for direct coating and film-forming process, and can be applied to a suspended online high-temperature curing process to improve production efficiency and reduce curling; fluorine-containing composite film can be used as a carrier for coating and film-forming process, without the need for lateral and The longitudinal stretching process reduces the process threshold; there is no oxygen content limit in the film-forming process, and the fluorine-containing composite film can be recycled multiple times, saving costs and conforming to the trend of environmental protection.
下面將結合具體實施例對本發明的技術方案進行清楚、完整地描述。顯然,所描述的實施方式僅是本發明一部分實施方式,而不是全部的實施方式。基於本發明中的實施方式,本領域普通技術人員在沒有做出創造性勞動前提下所獲得的所有其他實施方式,均屬於本發明保護的範圍。The technical solutions of the present invention will be clearly and completely described below with reference to specific embodiments. Obviously, the described embodiments are only some, but not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
除非另有定義,本文所使用的所有的技術和科學術語與屬於本發明的技術領域的技術人員通常理解的含義相同。在本發明的說明書中所使用的技術手段的名稱只是為了描述具體的實施例的目的,不是旨在於限制本發明。Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The names of technical means used in the description of the present invention are only for the purpose of describing specific embodiments, and are not intended to limit the present invention.
在不衝突的情況下,下述的實施例及實施例中的特徵可以相互組合。The embodiments described below and features in the embodiments may be combined with each other without conflict.
本發明提供了一種含氟分散液,該含氟分散液中包括含氟高分子粉體、第一溶劑和聚醯亞胺溶液,所述含氟高分子粉體的粒徑小於或等於3μm,所述聚醯亞胺溶液包括聚醯亞胺和第二溶劑,所述含氟高分子粉體和所述聚醯亞胺組成所述含氟分散液的固成分,所述含氟高分子粉體在所述含氟分散液的固成分中的重量百分比大於或等於85%,所述聚醯亞胺在所述含氟分散液的固成分中的重量百分比小於或等於15%。The present invention provides a fluorine-containing dispersion liquid, the fluorine-containing dispersion liquid includes a fluorine-containing polymer powder, a first solvent and a polyimide solution, and the particle size of the fluorine-containing polymer powder is less than or equal to 3 μm, The polyimide solution includes polyimide and a second solvent, the fluorine-containing polymer powder and the polyimide constitute the solid content of the fluorine-containing dispersion, and the fluorine-containing polymer powder The weight percentage of the polyimide in the solid content of the fluorine-containing dispersion is greater than or equal to 85%, and the weight percentage of the polyimide in the solid content of the fluorine-containing dispersion is less than or equal to 15%.
本實施方式中,所述含氟分散液的固含量為40wt%~50 wt%。In this embodiment, the solid content of the fluorine-containing dispersion liquid is 40 wt % to 50 wt %.
本實施方式中,所述含氟高分子粉體包括聚四氟乙烯、全氟烷氧基、聚全氟乙丙烯、三氟氯乙烯、乙烯-三氟氯乙烯及聚全氟亞乙烯基中的一種或幾種。In this embodiment, the fluorine-containing polymer powder includes polytetrafluoroethylene, perfluoroalkoxy, polyperfluoroethylene propylene, trifluorochloroethylene, ethylene-trifluorochloroethylene, and polyperfluoroethylene vinylene. one or more of them.
本實施方式中,所述第一溶劑和所述第二溶劑均為極性溶劑,具體可以是N-甲基吡咯烷酮(NMP)、二甲基乙醯胺(DMAC)、1,4-丁內酯(GBL),具體地,本實施方式中,所述第一溶劑和所述第二溶劑均為NMP。In this embodiment, the first solvent and the second solvent are both polar solvents, specifically N-methylpyrrolidone (NMP), dimethylacetamide (DMAC), 1,4-butyrolactone (GBL), specifically, in this embodiment, both the first solvent and the second solvent are NMP.
本實施方式中,所述含氟分散液還包括介面活性劑,所述介面活性劑採用傳統的介面活性劑,包括但不限於聚醚聚醯胺類、聚醚類、聚酯聚醯胺類、聚羧酸鈉鹽等介面活性劑,所述介面活性劑的添加能夠使得所述含氟高分子粉體均勻分散在所述第一溶劑中。In this embodiment, the fluorine-containing dispersion further includes a surfactant, and the surfactant adopts a traditional surfactant, including but not limited to polyether polyamides, polyethers, polyester polyamides , polycarboxylate sodium salt and other surfactants, the addition of the surfactant can make the fluorine-containing polymer powder uniformly dispersed in the first solvent.
本發明還提供了上述含氟分散液的製備方法,具體包括以下步驟:The present invention also provides a method for preparing the above-mentioned fluorine-containing dispersion, which specifically includes the following steps:
步驟S1,於反應容器內加入第一溶劑和介面活性劑,攪拌使兩者混合均勻。In step S1, the first solvent and the surfactant are added into the reaction vessel, and the mixture is stirred to make the two evenly mixed.
本實施方式中,所述第一溶劑為極性溶劑,具體可以是N-甲基吡咯烷酮(NMP)。In this embodiment, the first solvent is a polar solvent, specifically, N-methylpyrrolidone (NMP).
本實施方式中,所述介面活性劑採用傳統的介面活性劑,包括但不限於聚醚聚醯胺類、聚醚類、聚酯聚醯胺類、聚羧酸鈉鹽等介面活性劑。In this embodiment, the surfactant is a traditional surfactant, including but not limited to polyether polyamides, polyethers, polyester polyamides, and polycarboxylate sodium salts.
步驟S2,於步驟S1得到的混合溶液中加入含氟高分子粉體,混合得到第一混合液。In step S2, fluorine-containing polymer powder is added to the mixed solution obtained in step S1, and mixed to obtain a first mixed solution.
具體地,將所述含氟高分子粉體分批緩慢倒入步驟S1得到的混合液中,邊倒邊攪拌,至全部倒入,持續攪拌0.5h~24h時間,使含氟高分子粉體均勻分散在含有介面活性劑的第一溶劑中,得到第一混合液。Specifically, slowly pour the fluorine-containing polymer powder into the mixed solution obtained in step S1 in batches, stir while pouring, until all is poured, and continue to stir for 0.5h to 24h to make the fluorine-containing polymer powder It is uniformly dispersed in the first solvent containing the surfactant to obtain the first mixed solution.
所述含氟高分子粉體包括聚四氟乙烯(PTFE)、全氟烷氧基(PFA)、聚全氟乙丙烯(FEP)、三氟氯乙烯(CTFE)、乙烯-三氟氯乙烯(ECTFE)、及聚全氟亞乙烯基(PVDF)中的一種或幾種。The fluorine-containing polymer powder includes polytetrafluoroethylene (PTFE), perfluoroalkoxy (PFA), polyperfluoroethylene propylene (FEP), chlorotrifluoroethylene (CTFE), ethylene-chlorotrifluoroethylene ( ECTFE), and one or more of polyperfluorovinylidene (PVDF).
具體地,本實施方式中,所述含氟高分子粉體為全氟烷氧基(PFA)。Specifically, in this embodiment, the fluorine-containing polymer powder is perfluoroalkoxy (PFA).
本實施方式中,所述含氟高分子粉體的平均粒徑小於或等於3μm,優選為0.1μm~3μm。In the present embodiment, the average particle size of the fluorine-containing polymer powder is less than or equal to 3 μm, preferably 0.1 μm to 3 μm.
步驟S3,提供一聚醯亞胺溶液,並於所述第一混合液中加入所述聚醯亞胺溶液,混合得到所述含氟分散液。Step S3, providing a polyimide solution, adding the polyimide solution to the first mixed solution, and mixing to obtain the fluorine-containing dispersion.
其中所述含氟高分子粉體和所述聚醯亞胺組成所述含氟分散液的固成分,所述含氟高分子粉體在所述含氟分散液的固成分中的重量百分比大於或等於85%,所述聚醯亞胺在所述含氟分散液的固成分中的重量百分比小於或等於15%。The fluorine-containing polymer powder and the polyimide constitute the solid content of the fluorine-containing dispersion, and the weight percentage of the fluorine-containing polymer powder in the solid content of the fluorine-containing dispersion is greater than or equal to 85%, the weight percentage of the polyimide in the solid content of the fluorine-containing dispersion is less than or equal to 15%.
所述含氟分散液的膠體重量包括聚醯亞胺的重量、PFA粉體的重量以及溶劑NMP的重量,三者的重量百分比按100%計算,其中聚醯亞胺和PFA粉體為固體成分,得到的所述含氟分散液的膠體固含量為40wt%~50 wt%,黏度為500 CPS~1500 CPS。The colloidal weight of the fluorine-containing dispersion includes the weight of polyimide, the weight of PFA powder and the weight of solvent NMP, and the weight percentages of the three are calculated as 100%, wherein polyimide and PFA powder are solid components , the colloidal solid content of the obtained fluorine-containing dispersion liquid is 40 wt % to 50 wt %, and the viscosity is 500 CPS to 1500 CPS.
本實施方式中,所述聚醯亞胺溶液的製備方法包含以下步驟:In this embodiment, the preparation method of the polyimide solution comprises the following steps:
於反應容器中加入二胺、二酸酐及NMP溶劑,在氮氣環境下攪拌至少24小時,得到聚醯胺酸溶液。Diamine, dianhydride and NMP solvent were added to the reaction vessel, and the solution was stirred under nitrogen atmosphere for at least 24 hours to obtain a polyamide acid solution.
本實施方式中,聚醯胺酸溶液的固含量為 20wt%~25 wt%。In this embodiment, the solid content of the polyamic acid solution is 20 wt% to 25 wt%.
本實施方式中,所述二胺與所述二酸酐的摩爾比為1:1。In this embodiment, the molar ratio of the diamine to the dianhydride is 1:1.
本實施方式中,所述二胺為2,2-雙(3-氨基-4-羥基苯基)六氟丙烷(6FAP),所述二胺的質量為20g~40g,進一步優選24g~34g。In this embodiment, the diamine is 2,2-bis(3-amino-4-hydroxyphenyl)hexafluoropropane (6FAP), and the mass of the diamine is 20g-40g, more preferably 24g-34g.
本實施方式中,所述二酸酐為4,4'-(六氟異亞丙基)二鄰苯二甲酸酐(6FDA),所述二酸酐的質量為40g~55g。In this embodiment, the dianhydride is 4,4'-(hexafluoroisopropylidene)diphthalic anhydride (6FDA), and the mass of the dianhydride is 40g-55g.
第二步,於所述聚醯胺酸溶液中加入二甲苯(Xylene)溶劑,升溫至180℃於氮氣環境下進行環化反應,反應1h~6h,得到所述聚醯亞胺溶液。In the second step, xylene (Xylene) solvent is added to the polyimide solution, and the temperature is raised to 180° C. to carry out a cyclization reaction in a nitrogen environment, and the reaction is performed for 1 h to 6 h to obtain the polyimide solution.
本實施方式中,具體聚醯亞胺溶液製備方法中的反應過程如下所示: In the present embodiment, the reaction process in the specific polyimide solution preparation method is as follows:
請參閱圖1,本發明還提供一種含氟復合膜100,包括一基材1及設於所述基材1至少一表面的含氟膜2,所述含氟膜2藉由將如上所述的含氟分散液塗布於所述基材1的至少一面後加熱製成。Referring to FIG. 1 , the present invention further provides a fluorine-containing
本實施方式中,所述基材1為聚醯亞胺膜,所述基材1的厚度為125μm~225μm。聚醯亞胺膜厚度較厚,能夠提高所述含氟復合膜100的挺度和韌性。In this embodiment, the
本實施方式中,所述含氟膜2的厚度為3μm~6μm。In this embodiment, the thickness of the fluorine-containing
所述含氟膜2中包括所述含氟高分子粉體和聚苯惡唑,其中可以藉由調整所述含氟高分子粉體和聚苯惡唑的含量,來調節含氟復合膜的離型力。其中,含氟復合膜中的固體成分為含氟高分子粉體和聚苯惡唑,所述含氟高分子粉體在含氟復合膜中固成分的重量百分比大於或等於85%,所述聚苯惡唑在含氟復合膜中固成分的重量百分比小於或等於15%。所述含氟膜2中的含氟高分子粉體在高溫下會熔融變成熔體,便於成膜。The fluorine-containing
具體地,如上所述含氟復合膜的製備方法,包括以下步驟:Specifically, the above-mentioned preparation method of the fluorine-containing composite membrane includes the following steps:
第一步,提供聚醯亞胺薄膜,於所述聚醯亞胺薄膜的至少一面塗布如上所述的含氟分散液,得到中間體。In the first step, a polyimide film is provided, and the above-mentioned fluorine-containing dispersion is coated on at least one side of the polyimide film to obtain an intermediate.
第二步,將上述中間體於140℃~150℃的條件下進行烘烤。In the second step, the above intermediate is baked at a temperature of 140°C to 150°C.
第三步,將烘烤過的上述中間體於400℃~450℃的條件下進行燒結,得到所述含氟復合膜。In the third step, the baked intermediate is sintered at a temperature of 400° C. to 450° C. to obtain the fluorine-containing composite film.
由於在所述含氟分散液中添加有聚醯亞胺溶液,聚醯亞胺溶液在高溫下能夠進行熱重組(Thermally Rearranged , TR),原有的亞胺結構轉換成苯並惡唑結構,進而生成聚苯惡唑,反應過程如下所示: Because the polyimide solution is added to the fluorine-containing dispersion liquid, the polyimide solution can be thermally rearranged (TR) at high temperature, and the original imine structure is converted into a benzoxazole structure, And then generate polybenzoxazole, and the reaction process is as follows:
聚苯惡唑 (polybenzoxazole, PBO)是一種具有良好的熱性質及機械性質,和耐化學性的樹酯,結構類似於聚醯亞胺,但極性更低於聚醯亞胺,在含氟復合膜的表面具有聚苯惡唑成分,能夠很好地調節含氟復合膜的離型力大小,而且能夠更好地與中間的聚醯亞胺膜結合,提高含氟膜在基材上的附著力。Polybenzoxazole (PBO) is a resin with good thermal and mechanical properties, and chemical resistance. Its structure is similar to polyimide, but its polarity is lower than that of polyimide. The surface of the film has a polybenzoxazole component, which can well adjust the release force of the fluorine-containing composite film, and can better combine with the polyimide film in the middle to improve the adhesion of the fluorine-containing film to the substrate. force.
同時所述含氟高分子粉體顆粒也會在高溫條件下熔融,變成熔體,可以更好地均相成膜。At the same time, the fluorine-containing polymer powder particles are also melted under high temperature conditions to become a melt, which can better form a homogeneous film.
由於中間層的聚醯亞胺膜的厚度較厚,具有足夠的挺度和韌性,所以,燒結過程直接採用懸浮式(無滾輪)RTR(卷對卷)工藝或環化爐進行,且可減少捲曲現象。並且烘烤時無含氧量限制,符合環保趨勢。可藉由調整PFA粉體及聚苯惡唑的比例來改變含氟復合膜的離型力大小,進而增加後續製備聚醯亞胺薄膜時的配方選擇性。這裡調節PFA粉體及聚苯惡唑的比例具體可以在製備所述含氟分散液時藉由調節PFA粉體和聚醯亞胺的比例來控制。Because the thickness of the polyimide film in the middle layer is thick and has sufficient stiffness and toughness, the sintering process is directly carried out by a suspended (rollerless) RTR (roll-to-roll) process or a cyclization furnace, which can reduce the curling phenomenon. And there is no oxygen limit during baking, which is in line with the trend of environmental protection. The release force of the fluorine-containing composite film can be changed by adjusting the ratio of PFA powder and polybenzoxazole, thereby increasing the formulation selectivity in the subsequent preparation of the polyimide film. Here, adjusting the ratio of PFA powder and polybenzoxazole can be specifically controlled by adjusting the ratio of PFA powder and polyimide when preparing the fluorine-containing dispersion.
最終可製備一面具有所述含氟膜2或兩面具有所述含氟膜2的含氟復合膜100,當兩面皆有離型效果時,還可兩面塗布成膜,提高升產率,還可解決後續製備薄膜過程中層間沾黏等問題,並且含氟復合膜100為耐高溫材料( Td > 500℃),可以適用於高溫製程或含有高沸點溶劑的塗布成膜製程,而且烘烤時無含氧量限制,可多次使用,環保且節約成本。Finally, the fluorine-containing
本發明還提供一種聚合物薄膜的製備方法,包括以下步驟:The present invention also provides a preparation method of the polymer film, comprising the following steps:
步驟一,提供一聚合物溶液和如上所述的含氟復合膜100,所述含氟復合膜100包含至少一含氟膜2,於所述含氟膜2遠離所述基材1的表面塗布所述聚合物溶液並進行烘烤,從而形成一中間膜層。
步驟二,將所述中間膜層進行熟化,以形成所述聚合物薄膜。
所述聚合物溶液包括但不限於聚醯亞胺溶液、聚醯胺酸溶液或聚酯溶液等,具體地,本實施方式中,以聚醯胺酸溶液為例進行詳細說明。The polymer solution includes, but is not limited to, a polyimide solution, a polyamide solution, or a polyester solution, etc. Specifically, in this embodiment, a polyamide solution is used as an example for detailed description.
具體生產聚醯亞胺薄膜的方法可以採用以下兩種方式,這兩種方式最主要的區別是熟化過程會有區別,一種的熟化過程是採用傳統批次式整卷放入氮氣高溫環境下進行熟化;另一種方式是採用懸浮式(無滾輪)的RTR烘箱及高溫環化爐直接線上熟化。其中第一種方式通常用於單面覆膜的生成情況,另一種方式可以雙面覆膜,生成效率更高。藉由這種方式生成聚醯亞胺薄膜可控制聚合物薄膜厚度至更薄,而且適用於易脆裂或熱塑性的聚醯酸胺溶液的成膜。The specific production method of polyimide film can be carried out in the following two ways. The main difference between the two methods is that the curing process will be different. One kind of curing process is to use the traditional batch type whole roll and put it in a high temperature nitrogen environment. Curing; another way is to use a suspended (no roller) RTR oven and a high-temperature cyclization furnace for direct on-line curing. The first method is usually used for the production of single-sided film, and the other method can be double-sided film, and the production efficiency is higher. The polyimide film produced in this way can control the thickness of the polymer film to be thinner, and is suitable for the film formation of brittle or thermoplastic polyimide solutions.
下面結合圖2對第一種方式進行詳細說明:The first method will be described in detail below in conjunction with Figure 2:
首先所述含氟復合膜100的兩面均為含氟膜面,以所述含氟復合膜100為承載體,於任一所述含氟膜面塗布聚醯胺酸溶液,並進行烘烤,以在所述含氟膜面形成一聚醯胺酸膜200。First, both sides of the fluorine-containing
再將所述聚醯胺酸膜200和所述含氟復合膜100一起整體收卷,得到半成品卷膜。Then, the
將半成品卷膜放入在250℃~360℃的烘箱中,通入氮氣,進行熟化,使聚醯胺酸膜200進行高溫環化,進而形成聚醯亞胺薄膜300。The semi-finished roll film is put into an oven at 250°C to 360°C, and nitrogen gas is introduced for curing, so that the
將整卷膜在撕膜機上將所述含氟復合膜100和聚醯亞胺薄膜300分別收卷,便得到成品的聚醯亞胺薄膜300卷料。The fluorine-containing
聚醯胺酸薄膜於批次烘箱放卷熟化時,含氟復合膜單面塗布聚醯胺酸,因含氟復合膜兩面皆有離型力,成功改善卷料層間沾黏性的問題,並且可一次多捲進行高溫環化,提高生產效率。When the polyamide film is unrolled and matured in a batch oven, the fluorine-containing composite film is coated with polyamide on one side. Because the fluorine-containing composite film has a release force on both sides, the problem of interlayer adhesion of the roll material is successfully improved, and the High temperature cyclization can be carried out for multiple rolls at a time to improve production efficiency.
下面結合圖3對第一種方式進行詳細說明:The first method will be described in detail below with reference to Figure 3:
首先所述含氟復合膜100的兩面均為含氟膜面,以所述含氟復合膜100為承載體,在所述含氟復合膜100的至少一面塗布聚醯胺酸溶液,並進行烘烤,以在所述含氟膜面形成一聚醯胺酸膜200。First, both sides of the fluorine-containing
再將一面或兩面具有聚醯胺酸膜200的所述含氟復合膜100採用懸浮式(無滾輪)RTR烘箱於250℃~360℃的氮氣環境下進行線上熟化,使聚醯胺酸膜200進行高溫環化,進而形成聚醯亞胺薄膜300。Then, the fluorine-containing
將聚醯亞胺薄膜300和所述含氟復合膜100分別收卷,便得到成品的聚醯亞胺薄膜300卷料。The
採用這種方式可以同時生產兩卷料,提升了產能。In this way, two rolls of material can be produced at the same time, which increases the production capacity.
由於含氟復合膜100耐高溫,適用於聚醯亞胺薄膜的成膜製程;含氟復合膜100可實現雙面離型,適用於傳統的批次成卷高溫熟化,避免成卷熟化過程中層間沾黏等問題,同時雙離型面可以同時成膜,提高了生產效率;由於含氟復合膜100位於中間層的聚醯亞胺膜的厚度較厚,具有足夠的挺度和韌性,可採用含氟復合膜100作為承載體直接進行塗布成膜製程,且可適用於懸浮式線上高溫熟化製程,提高生產效率,且可減少捲曲現象;可採用含氟復合膜100作為承載體進行塗布成膜製程,無需橫向及縱向拉伸過程,降低了製程門檻;成膜製程中無含氧量限制,且含氟復合膜100可以多次回收利用,節約成本,同時符合環保趨勢。Because the fluorine-containing
以下藉由具體實施例來對本申請的方案進行進一步說明。The solution of the present application will be further described below with specific examples.
合成例1Synthesis Example 1
於500ml反應瓶中加入二胺(6FAP 33.89g)和二酸酐(6FDA 41.11g),其中二胺和二酸酐的摩爾比為1:1,溶劑NMP(225g),其中固含量為20wt%~25wt%,於氮氣環境下攪拌24小時,再加入二甲苯(45g),並升溫至180℃於氮氣環境下攪拌6小時,進行除水環化,得到聚醯亞胺溶液。In a 500ml reaction flask, add diamine (6FAP 33.89g) and dianhydride (6FDA 41.11g), wherein the molar ratio of diamine and dianhydride is 1:1, solvent NMP (225g), wherein the solid content is 20wt% ~ 25wt %, stirred for 24 hours in a nitrogen atmosphere, then added xylene (45 g), and heated to 180° C. and stirred for 6 hours in a nitrogen atmosphere to remove water and cyclize to obtain a polyimide solution.
合成例2Synthesis Example 2
於500ml反應瓶中加入二胺(3,3'-二羥基聯苯胺HAB 24.55g)和二酸酐(6FDA 50.45g) 其中二胺和二酸酐的摩爾比為1:1,溶劑NMP(225g),其中固含量為20wt%~25wt%,於氮氣環境下攪拌24小時,再加入二甲苯(45g),並升溫至180℃於氮氣環境下攪拌6小時,進行除水環化,得到聚醯亞胺溶液。In a 500ml reaction flask, add diamine (3,3'-dihydroxybenzidine HAB 24.55g) and dianhydride (6FDA 50.45g) wherein the molar ratio of diamine and dianhydride is 1:1, solvent NMP (225g), Wherein the solid content is 20wt%~25wt%, stir under nitrogen environment for 24 hours, then add xylene (45g), and heat up to 180 ℃ and stir under nitrogen environment for 6 hours, carry out dewatering and cyclization to obtain polyimide solution.
實施例1Example 1
於500mL反應瓶分別加入NMP(45g)、介面活型劑(5g),進行攪拌至均勻分散,再將含氟高分子粉體PFA (粒徑<3μm,50g)分批緩慢倒入上述溶液中,並同時攪拌至全數倒入,持續攪拌24小時,即配製完成未添加聚醯亞胺溶液的氟分散液。Add NMP (45g) and surfactant (5g) to a 500mL reaction flask, stir until uniformly dispersed, and then slowly pour the fluorine-containing polymer powder PFA (particle size <3μm, 50g) into the above solution in batches , and at the same time, stir until all is poured in, and continue to stir for 24 hours, that is, the fluorine dispersion without adding the polyimide solution is prepared.
實施例2Example 2
於100mL反應瓶分別加入實施例1製備的氟分散液(30.4g),進行攪拌,同時緩慢加入合成例1(3.2g),持續攪拌24小時,即配製完成含氟分散液。The fluorine dispersion liquid (30.4g) prepared in Example 1 was respectively added to the 100mL reaction flask, and stirred, and at the same time, Synthesis Example 1 (3.2g) was slowly added, and the stirring was continued for 24 hours, that is, the fluorine-containing dispersion liquid was prepared.
實施例3Example 3
於100mL反應瓶分別加入實施例1製備的氟分散液(28.8g),進行攪拌,同時緩慢加入合成例1製備的聚醯亞胺溶液(6.4g),持續攪拌24小時,即配製完成含氟分散液。The fluorine dispersion (28.8g) prepared in Example 1 was respectively added to the 100mL reaction flask, and stirred, and the polyimide solution (6.4g) prepared in Synthesis Example 1 was slowly added at the same time, and the stirring was continued for 24 hours, that is, the fluorine-containing solution was prepared. Dispersions.
實施例4Example 4
於100mL反應瓶分別加入實施例1製備的氟分散液(27.2g),進行攪拌,同時緩慢加入合成例1製備的聚醯亞胺溶液(9.6g),持續攪拌24小時,即配製完成含氟分散液。The fluorine dispersion (27.2g) prepared in Example 1 was respectively added to the 100mL reaction flask, stirred, and the polyimide solution (9.6g) prepared in Synthesis Example 1 was slowly added at the same time, and the stirring was continued for 24 hours, that is, the fluorine-containing solution was prepared. Dispersions.
對比例1Comparative Example 1
與實施例1的區別在於,含氟高分子粉體PFA 的粒徑為4~6μm。The difference from Example 1 is that the particle size of the fluorine-containing polymer powder PFA is 4 to 6 μm.
對比例2Comparative Example 2
與實施例2的區別在於,用對比例1製備的氟分散液(30.4g)取代實施例1製備的氟分散液。The difference from Example 2 is that the fluorine dispersion prepared in Example 1 was replaced with the fluorine dispersion prepared in Comparative Example 1 (30.4 g).
對比例3Comparative Example 3
與實施例2的區別在於,用350℃進行烘烤。The difference from Example 2 is that baking is performed at 350°C.
對比例4Comparative Example 4
與實施例2的區別在於,用合成例2合成的聚醯亞胺溶液(3.2g)取代合成例1合成的聚醯亞胺溶液。The difference from Example 2 is that the polyimide solution (3.2 g) synthesized in Synthesis Example 2 was used instead of the polyimide solution synthesized in Synthesis Example 1.
對比例5Comparative Example 5
於100mL反應瓶分別加入實施例1製備的氟分散液(25.6g),進行攪拌,同時緩慢加入合成例1(12.8g),持續攪拌24小時,即配製完成含氟分散液。The fluorine dispersion liquid (25.6g) prepared in Example 1 was respectively added to the 100mL reaction flask, and stirred, and at the same time, Synthesis Example 1 (12.8g) was slowly added, and the stirring was continued for 24 hours, that is, the fluorine-containing dispersion liquid was prepared.
其中,實施例1-4和對比例1-5的配方和製備條件及性能如表1所示。Wherein, the formulas, preparation conditions and properties of Examples 1-4 and Comparative Examples 1-5 are shown in Table 1.
表1
注:表1中PFA 粉體和聚醯亞胺的比例是以PFA 粉體和聚醯亞胺在含氟分散液中固成分的重量比例計算。Note: The ratio of PFA powder and polyimide in Table 1 is calculated based on the weight ratio of the solid content of PFA powder and polyimide in the fluorine-containing dispersion.
含氟高分子粉體的粒徑測試採用ASTM D1210標準。The particle size test of fluorine-containing polymer powder adopts ASTM D1210 standard.
離型力測試採用ASTM D3330標準。The release force test adopts ASTM D3330 standard.
離型力-測試方式:室溫下測試,4.5lb滾輪輾壓,180°,300mm/min peel,測試標準樣採用的是日東31B。Release force - test method: test at room temperature, 4.5lb roller rolling, 180°, 300mm/min peel, the test standard is Nitto 31B.
測試結果表明:由實施例1和對比例1,可知本發明中的氟分散液中含氟高分子粉體(具體為PFA粉體)粒徑需小於或等於3μm,原因是,當PFA粉體的粒徑大於3後,含氟分散液易產生沉降、塗布時出現厚度不均的現象,而且在高溫熔融時,而且粒徑大於3μm的PFA粉體顆粒無法完全熔融,導致無法均相成膜。The test results show that: from Example 1 and Comparative Example 1, it can be seen that the particle size of the fluorine-containing polymer powder (specifically PFA powder) in the fluorine dispersion in the present invention needs to be less than or equal to 3 μm, the reason is that when the PFA powder When the particle size is larger than 3, the fluorine-containing dispersion is prone to sedimentation and uneven thickness during coating, and when melted at high temperature, PFA powder particles with a particle size larger than 3 μm cannot be completely melted, resulting in inability to form a homogeneous film .
由實施例1-4可知,藉由調整聚醯亞胺溶液和PFA粉體的添加比例,可以控制最終成型的含氟復合膜的離型力,由表1中離型力資料可以看出,聚醯亞胺溶液的添加量越大,最終含氟復合膜的離型力越大。原因是,聚醯亞胺在高溫條件下會生成聚苯惡唑,而聚苯惡唑和PFA粉體的極性存在一定的差異,藉由調整兩者的比例,可以很好地控制最終含氟復合膜的離型力大小,進而增加聚醯亞胺薄膜制膜過程中聚醯胺酸或其它樹酯配方選擇性,並且聚苯惡唑和PFA粉體皆有良好熱性質(Td5% > 500℃ ),適用於高溫製程。It can be seen from Examples 1-4 that the release force of the final formed fluorine-containing composite film can be controlled by adjusting the addition ratio of the polyimide solution and the PFA powder. It can be seen from the release force data in Table 1 that, The larger the added amount of the polyimide solution, the greater the release force of the final fluorine-containing composite membrane. The reason is that polyimide will generate polybenzoxazole under high temperature conditions, and the polarity of polybenzoxazole and PFA powder is different to a certain extent. By adjusting the ratio of the two, the final fluorine content can be well controlled. The release force of the composite film increases the selectivity of polyimide or other resin formulations in the process of polyimide film production, and both polybenzoxazole and PFA powder have good thermal properties (Td5%> 500 ℃ ), suitable for high temperature process.
由對比例2和實施例2可知,對比例2中出現團聚及相分離現象,原因是PFA粉體的顆粒粒徑過大,含氟分散液易產生沉降、塗布時出現厚度不均的現象。It can be seen from Comparative Example 2 and Example 2 that the phenomenon of agglomeration and phase separation occurs in Comparative Example 2, because the particle size of the PFA powder is too large, the fluorine-containing dispersion is prone to sedimentation, and the thickness is uneven during coating.
由對比例3和實施例2可知由於合成例1的聚醯亞胺溶液,具有羥基(-OH) ,其中羥基為極性官能團,於高溫350℃燒結成膜時,由於350℃未到達聚醯亞胺溶液的熱重組溫度,因此對比例3中的聚醯亞胺溶液未發生熱重組,對比例3中聚醯亞胺溶液與粒徑過大的PFA粉體極性差異過大,造成團聚,容易產生相分離現象。It can be seen from Comparative Example 3 and Example 2 that since the polyimide solution of Synthesis Example 1 has hydroxyl groups (-OH), the hydroxyl groups are polar functional groups. The thermal recombination temperature of the amine solution, so the polyimide solution in Comparative Example 3 did not undergo thermal recombination. separation phenomenon.
由對比例4和實施例2可知,因合成例2的二胺單體選用HAB,不含氟元素,相對合成例1,含氟元素的比例較低,進而造成對比例4中聚醯亞胺與PFA粉體的相容性下降,導致兩者無法相容,因此,對比例4在塗布成膜及高溫燒結後,目測可看出相分離現象。As can be seen from Comparative Example 4 and Example 2, because the diamine monomer of Synthesis Example 2 is selected from HAB and does not contain fluorine elements, relative to Synthesis Example 1, the ratio of fluorine-containing elements is relatively low, thereby causing polyimide in Comparative Example 4. The compatibility with PFA powder decreased, resulting in the incompatibility between the two. Therefore, after coating film formation and high temperature sintering in Comparative Example 4, the phase separation phenomenon can be seen visually.
對比例5中目測可觀察出相分離現象,無法均相成膜,並且離型力測試無再現性資料。藉由將對比例5與實施例1-4進行比較,可知出現上述現象的原因是,由於其添加聚醯亞胺的量過多,於塗布成膜及高溫燒結後形成的聚苯惡唑的添加量超過15%,而PFA粉體的極性低於聚苯惡唑的極性,這樣,由於兩者極性差異過大,造成了相分離,無法均相成膜,並且離型力測試無再現性(由離型力測試可驗證)。另外,聚苯惡唑的添加量大於15%(固體重量比例),會造成聚苯惡唑團聚,無法均勻分散於PFA粉體熔融後的熔體中,進而阻礙PFA高溫熔融成膜,無法成連續相而造成相分離及孔洞。In Comparative Example 5, the phase separation phenomenon could be observed visually, and the film could not be homogeneously formed, and there was no reproducible data in the release force test. By comparing Comparative Example 5 with Examples 1-4, it can be seen that the reason for the above phenomenon is that due to the excessive amount of polyimide added, the addition of polybenzoxazole formed after coating film formation and high temperature sintering. The amount of PFA powder exceeds 15%, and the polarity of PFA powder is lower than that of polybenzoxazole. In this way, due to the large difference in polarity between the two, the phase separation is caused, and the homogeneous film cannot be formed, and the release force test has no reproducibility (by Release force test can be verified). In addition, the addition amount of polybenzoxazole is more than 15% (solid weight ratio), which will cause polybenzoxazole to agglomerate, which cannot be uniformly dispersed in the melt after the PFA powder is melted, thereby hindering the high-temperature melting of PFA and forming a film, which cannot be formed into a film. The continuous phase causes phase separation and voids.
綜上所述,本發明的有益效果在於:含氟復合膜中由於聚苯惡唑的存在,保有耐高溫特性,使含氟復合膜在高溫條件下依然具有離型力,適用於高溫製程或含有高沸點溶劑的塗布成膜製程;可藉由調整含氟高分子粉體和聚苯惡唑的比例,可以調整含氟復合膜的離型力大小,適用於對離型力有不同要求的多種聚合物溶液成膜,提高了聚合物溶液的配方選擇性;含氟復合膜可實現雙面離型,適用於傳統的批次成卷高溫熟化,避免成卷熟化過程中層間沾黏等問題,同時雙離型面可以同時成膜,提高了生產效率;由於含氟復合膜位於中間層的聚醯亞胺膜的厚度較厚,具有足夠的挺度和韌性,可採用含氟復合膜作為承載體直接進行塗布成膜製程,且可適用於懸浮式線上高溫熟化製程,提高生產效率,且可減少捲曲現象;可採用含氟復合膜作為承載體進行塗布成膜製程,無需橫向及縱向拉伸過程,降低了製程門檻;成膜製程中無含氧量限制,且含氟復合膜可以多次回收利用,節約成本,同時符合環保趨勢。To sum up, the beneficial effects of the present invention are: due to the existence of polybenzoxazole in the fluorine-containing composite film, the high temperature resistance is maintained, so that the fluorine-containing composite film still has the release force under high temperature conditions, which is suitable for high temperature process or Coating and film-forming process containing high boiling point solvent; by adjusting the ratio of fluorine-containing polymer powder and polybenzoxazole, the release force of the fluorine-containing composite film can be adjusted, which is suitable for different requirements for release force. Various polymer solutions are used to form films, which improves the formulation selectivity of polymer solutions; fluorine-containing composite films can realize double-sided release, which is suitable for traditional batch high-temperature curing in rolls, avoiding problems such as interlayer sticking during roll curing. At the same time, the double release surface can form a film at the same time, which improves the production efficiency; because the thickness of the polyimide film with the fluorine-containing composite film in the middle layer is thick and has sufficient stiffness and toughness, the fluorine-containing composite film can be used as the film. The carrier is directly coated and film-forming, and can be applied to the suspended online high-temperature curing process to improve production efficiency and reduce curling. The stretching process reduces the process threshold; there is no oxygen content limit in the film-forming process, and the fluorine-containing composite film can be recycled multiple times, saving costs and conforming to the trend of environmental protection.
以上實施例和對比例的說明只是用於幫助理解本發明的方法及其核心思想;另外,對於本領域的普通技術人員來說,可以根據本發明的技術構思做出其它各種相應的改變與變形,而所有這些改變與變形均應屬於本發明請求項的保護範圍。The descriptions of the above embodiments and comparative examples are only used to help understand the method of the present invention and its core idea; in addition, for those of ordinary skill in the art, various other corresponding changes and modifications can be made according to the technical idea of the present invention , and all these changes and deformations should belong to the protection scope of the claims of the present invention.
100:含氟復合膜 1:基材 2:含氟膜 200:聚醯胺酸膜 300:聚醯亞胺薄膜100: Fluorine-containing composite membrane 1: Substrate 2: Fluorine-containing film 200: Polyamide film 300: Polyimide film
圖1是本發明一實施方式提供的含氟復合膜的製備流程圖。FIG. 1 is a flow chart of the preparation of the fluorine-containing composite membrane provided by an embodiment of the present invention.
圖2是本發明一實施方式提供的薄膜的製備流程圖。FIG. 2 is a flow chart of the preparation of the thin film provided by an embodiment of the present invention.
圖3是本發明另一實施方式提供的薄膜的製備流程圖。FIG. 3 is a flow chart of the preparation of the thin film provided by another embodiment of the present invention.
100:含氟復合膜100: Fluorine-containing composite membrane
1:基材1: Substrate
2:含氟膜2: Fluorine-containing film
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