TW200914255A - Optical film having reduced size and number of gels and manufacturing method thereof - Google Patents

Optical film having reduced size and number of gels and manufacturing method thereof Download PDF

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Publication number
TW200914255A
TW200914255A TW097132586A TW97132586A TW200914255A TW 200914255 A TW200914255 A TW 200914255A TW 097132586 A TW097132586 A TW 097132586A TW 97132586 A TW97132586 A TW 97132586A TW 200914255 A TW200914255 A TW 200914255A
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Taiwan
Prior art keywords
film
alicyclic
resin
specific energy
gels
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TW097132586A
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Chinese (zh)
Inventor
Bang-Duk Kim
Chang-Gyu Im
Jin-Woo Lee
Sun-Ae Hwang
Sei-Jin Oh
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Cheil Ind Inc
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Publication of TW200914255A publication Critical patent/TW200914255A/en

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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
    • 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
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/08Copolymers of ethene
    • C08L23/0807Copolymers of ethene with unsaturated hydrocarbons only containing more than three carbon atoms
    • C08L23/0815Copolymers of ethene with aliphatic 1-olefins
    • C08L23/0823Copolymers of ethene with aliphatic cyclic olefins
    • GPHYSICS
    • G02OPTICS
    • G02BOPTICAL ELEMENTS, SYSTEMS OR APPARATUS
    • G02B1/00Optical elements characterised by the material of which they are made; Optical coatings for optical elements
    • G02B1/04Optical elements characterised by the material of which they are made; Optical coatings for optical elements made of organic materials, e.g. plastics
    • 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
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/04Homopolymers or copolymers of ethene
    • C08J2323/08Copolymers of ethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/16Applications used for films

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  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Health & Medical Sciences (AREA)
  • Materials Engineering (AREA)
  • General Physics & Mathematics (AREA)
  • Optics & Photonics (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Liquid Crystal (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Polarising Elements (AREA)

Abstract

An optical film for realizing excellent surface characteristics and a method for manufacturing the same are disclosed. Accordingly, an optical film having reduced size and number of gels by controlling the specific energy in the process of melt extrusion of the resin, and a manufacturing method of the film are provided. Thusly manufactured optical film can be widely utilized in manufacturing display products such as LCDs.

Description

200914255200914255

File:TW478IF 九、發明說明: 【發明所屬之技術領域】 本發色的表面特性之光學薄膜 f更特別地’為有關—具有減少凝膠尺寸及數 目之光學薄膜與其製造方法。 【先前技術】 因薄型螢幕如LCD及PDP具有增加的需求,並 先學溥膜的需求快速增加。 八兀件如 學算而式嗝使用於逆些產口口的薄膜需要光 :或w的相位差。_地,❹於大⑽ 要咼均一性的光學特性。 、而 位差:ί二Γ板需要—薄膜以補償通過液晶的光之相 廣視角。這些相位差薄膜在除了均-的 必須在薄膜表面凝膠具有最小的缺陷及少數 傳統相位差薄膜藉由在三 晶或經拉伸賦予相位差至 上塗覆液 十上," α曰®义纖維素溥臈而製造。折 :’相位巧_由拉伸脂環稀烴 系相位差。 ^ $代纖維素 用以製造上述薄光學薄膜之典型方法 鑄方法完成’其中聚八物、,容於、'六 使用命剑》〇 可_性帶上 σ / 、/合训中,此生成溶液塗佈於 =色:=此造具有均-厚 空氣下回收且生產速度相對於高成;:==至 200914255File: TW478IF IX. Description of the Invention: [Technical Field of the Invention] The optical film f of the surface characteristics of the present color development is more specifically related to an optical film having a reduced gel size and number and a method for producing the same. [Prior Art] Due to the increased demand for thin screens such as LCDs and PDPs, the demand for enamel film has increased rapidly. Eight-piece pieces, such as calculations, are used to reverse the film of the mouth to require a light: or w phase difference. _ ground, ❹大 (10) The optical properties of uniformity. And the difference: ί Γ 需要 requires a film to compensate for the wide viewing angle of light passing through the liquid crystal. These retardation films have the smallest defects in the gel on the surface of the film except for the uniformity, and a few conventional retardation films impart a phase difference to the upper coating liquid by three crystals or by stretching, " α曰® Made from cellulose. Fold: 'Phase is _ from the stretched alicyclic hydrocarbon system phase difference. ^ $Cellulose is used to make the above-mentioned thin optical film. The typical method of casting is to complete the 'integrated eight objects, the capacity, the 'six use the sword', the _ sex band on σ / , / training, this generation The solution is applied to = color: = this is produced with uniform-thick air and the production speed is relative to high;; == to 200914255

Fiie:TW478IF 的,因而降低經濟效率。 一在此事件上,薄膜生產者已經嘗試在薄膜 :炼融擠出方法而獲得出色的光學特性上進行研::良 ’Ippmi ZeQn公司已將—脂 九口 而製造的薄獏商業化。 树如進仃熔融擠出 在脂環稀烴樹脂以相位差薄膜商業化後 :::開發相位差薄膜,其係在低成本使用—脂環稀= 終在溶融擠出f程加I共聚合物最 此,限制住使用脂環稀烴共聚合物 J=J因 應用。 v王而罟呵口口質顯示器的 為解決上述問題,本發明發明人已投入 t凝膠的尺寸及數目。因此,已開發出用於製造=出 =㈣性之_的製程,同時維持—高產能發 於此些發現而完成。 个U暴 【發明内容】 =此’本發縣於上述問題完成,且本發明目的是提 色表面特性的光學薄膜’其中薄膜為脂環烯烴共 來句製成且在64〇μπΐχ48〇μιη單位面積具有尺寸為邛 pm或更大的凝膠數為小於1.5。 ^,外,本發明之另一目的提供製造光學薄膜的方法, 其,藉,在一熔融擠出製程中以0.14 kWh/kg或更低的 特毛此里擠壓脂裱烯烴共聚合物,其中特定能量為在擠 200914255Fiie: TW478IF, thus reducing economic efficiency. At this event, film producers have attempted to develop excellent optical properties in the film: smelting extrusion process: Good ‘Ippmi ZeQn has commercialized 貘 九 九 。. The tree is melted and extruded in an alicyclic dilute resin and commercialized with a phase difference film::: Development of a phase difference film, which is used at low cost - alicyclic dilution = final melt extrusion, f-pass, I-copolymerization Most of this, the use of alicyclic dilute copolymer J=J is limited. v The king's mouth and mouth display In order to solve the above problems, the inventors of the present invention have invested in the size and number of t gels. Therefore, a process for manufacturing = out = (four) is developed, while maintaining - high capacity is achieved by these findings. U violent [experimental content] = This 'Beneficial County completed the above problems, and the object of the present invention is to improve the surface properties of the optical film 'where the film is made of alicyclic olefins and is in the range of 64 〇μπΐχ48〇μηη The number of gels having an area of 邛 pm or larger is less than 1.5. In addition, another object of the present invention is to provide a method of producing an optical film by extruding a lipid oxime olefin copolymer at a specific hair of 0.14 kWh/kg or less in a melt extrusion process. Which specific energy is in the crowd 200914255

File:TW4781F 壓機-中螺桿轉動之工作電能除以每小時的擠壓機輸 出。 依據本發明之一態樣,上述及其他目的可藉由具有出 色表則寺性的光學薄膜之提供而達成,其中薄膜由脂環稀 煙共聚物製成且在640μηΐ X 48G μηι單位面積具有尺寸為 30 μηΊ或更大的凝膠數為小於丨5。 ::本發明之另一態樣,上述及其他目的可藉由提 D 學㈣之方法而達成,其係藉由在-炫融擠出繁 =以二或更低的特定能量_旨環烯烴共 除以母小時的擠壓機輸出。 电月匕 ^本务明之上述及其他目❸、特徵及其 列詳細描述配合附圖而更清楚瞭解。 ’·、 ' 【實施方式】 i 現在,將進一步詳述本發明。 使用於顯示產品之光學薄膜的表 ,期間於一_機與滾筒或皮帶的黏著而^吊=在製 常發生的情況為在高廢、溫度 、二、而,時 變形而產生的凝膠或烴類。 厚4下通過擠壓機時經 不像脂環稀烴樹脂,脂環稀烴共 杨相同於聚乙稀者,因此其很容易:有-主鏈結構 制脂環稀烴共聚合物應用至光學薄膜。乂轉。因此,限 已知當樹脂在_機中部份降解時且當交聯由降解 200914255File: TW4781F Press - The operating energy of the screw in the middle of the screw divided by the output of the extruder per hour. According to one aspect of the present invention, the above and other objects are attained by the provision of an optical film having an excellent surface which is made of an alicyclic smoke copolymer and has a size per unit area of 640 μηΐ X 48 G μηι. The number of gels of 30 μηΊ or larger is less than 丨5. According to another aspect of the present invention, the above and other objects can be attained by the method of the above-mentioned D (4), which is carried out by extruding and melting a specific energy of two or less. Divided by the output of the extruder at the parent hour. The above and other objectives, features and detailed descriptions of the present invention are more clearly understood in conjunction with the accompanying drawings. ‘·· ' [Embodiment] i The present invention will now be described in further detail. A watch used to display an optical film of a product, during which the adhesion of a machine to a roller or a belt is hanged. In the case where the system is often produced, the gel is generated by deformation at high waste, temperature, and time. Hydrocarbons. When the thickness is 4, it is not like the alicyclic dilute resin when passing through the extruder. The alicyclic hydrocarbon is the same as the polyethylene, so it is easy: the -chain structure of the alicyclic dilute copolymer is applied to Optical film. Twirling. Therefore, it is known that when the resin is partially degraded in the machine and when the crosslinking is degraded by 200914255

File:TW478IF 作用而產生的自由基連續反應進行時, 因此形成的凝膠在位於薄膜表面/ 突出之錐狀。另一方面,凝膠為部份 、/、 一由表面 為類似故有時候稱為魚眼。此此 ^ ’且其橫切面因 射率,因此凝膠當嵌在薄膜内;==相同_ 當存在於表面時被認為是主要缺陷。、一而疑曝 凝膠可被-細濾網移除。然 形成時必需時常清潔而不便。另一問:^在當多凝耀數 成的凝膠不能被移除。另_ =顧製程後形 !純物的例子…率不同於樹:::脂=: 由位於觸中段的細滤 提出 = 開第 2000-233425 及 2006一096001 號 =、,§、纟财脂料烴絲財娜的形成具 壓縮比例本身的降低不旦^本毛明發明人的研究,觀察到 參照各圖示,*在;;= 尺寸及數目的降低。 進行壓縮時延長以^^圖中的螺桿區段1的長度在 ^ , , X于比弟h圖中的螺桿為相對低的壓 =部:::=r間產生摩擦處延長該段落。因 降低:心 在擠:二程中樹脂吸收能量。此能量可區分為 旦。奋士 產生的熱能及由螺桿轉動產生的物理能 里田^明之脂環烯烴共聚物在擠壓機中只佔用一小段 200914255File: The continuous reaction of free radicals generated by the action of TW478IF is carried out, so that the gel formed is in the shape of a cone/projection on the surface of the film. On the other hand, the gel is part, /, and the surface is similar, sometimes called fisheye. Thus ^ ' and its cross-section is incident, so the gel is embedded in the film; == the same _ is considered to be the main defect when present on the surface. The suspected gel can be removed by the fine filter. However, it must be cleaned and inconvenient at the time of formation. Another question: ^ When the gel that is condensed is not removed. Another _ = Gu after the shape! Pure example of the ... rate is different from the tree :::: = = by the fine filter located in the middle of the touch = open 2000-233425 and 2006 096001 =,, §, 纟 脂 fat The formation of the hydrocarbon sylvestre has a reduction in the compression ratio itself. In the study of the inventor of the present invention, it has been observed to refer to the respective figures, * in;; = reduction in size and number. When the compression is performed, the length of the screw section 1 in the figure is extended at ^ , and X is a relatively low pressure in the screw of the figure h = part::: = r creates a friction between the paragraphs to extend the paragraph. Because of the reduction: the heart is squeezed: the resin absorbs energy in the second pass. This energy can be distinguished as a denim. The heat energy generated by Fenshi and the physical energy produced by the rotation of the screw. The alicyclic olefin copolymer of Rita Yuming only takes up a short section in the extruder. 200914255

Fi!e:TW478IF ^ 3卩使”聚物暴露在高溫下,未觀察到凝勝的形成。 可知物理能量在脂環稀烴共聚物樹脂中於 上比熱能參予更多。 ==物理能量可藉由計算特定能量而獲得。特 月二二::轉動使用的能量除以每小時的擠壓機輸出。 ㈣定義為一在螺桿馬達中炫融擠壓1 ^樹脂Fi!e: TW478IF ^ 3卩 The polymer was exposed to high temperatures and no formation of condensate was observed. It is known that the physical energy is more involved in the upper specific heat energy in the alicyclic dilute copolymer resin. It can be obtained by calculating the specific energy. The special month 22:: the energy used for the rotation divided by the output of the extruder per hour. (4) Defined as a squeeze in the screw motor 1 ^ resin

的使用月巧為kWh/kg。特定能量顯示於下列方程式。 t方程式J 輸出kWh/kg指(kg/hr )=螺桿馬達電能/每小時的擠壓機 ==量可因製程條件如擠出溫度、螺桿的旋轉速 人或進料系統變化。此外裤 脂單體的組成。特疋Μ也會因螺桿設計或樹 本發明之發明人發現特定能量本身為決定凝膠形成 的於變化特定能量之因素。即,發現凝膠 勺尺寸及數目(形成及成長)可拉山—Λ ^ 的特定能量擠壓樹脂而實質降^。 . kwh/kg或更低 當特定能量低於〇. 14 kWh/iro· 〇 ,Λ 1單:立面積中一具有尺寸為3Q㈣的凝膠數可降::::^ 薄膜表且面 ZD此—凝膠量程度評做為利於光學 同時,當特定能量超過〇.14 kWh/kg,樹 在分子鍵的部份降解期間自由基產生的過量剪/ 力。因此’可促進凝膠的形成及成長。 y應The monthly usage is kWh/kg. The specific energy is shown in the equation below. t Equation J Output kWh/kg means (kg/hr) = screw motor power / hourly extruder = = amount can vary due to process conditions such as extrusion temperature, screw speed or feed system. In addition, the composition of the trousers monomer. In particular, the inventors of the present invention have discovered that the specific energy itself is a factor that determines the specific energy of the gel formation. That is, it was found that the size and number (formation and growth) of the gel spoon can be substantially reduced by the specific energy of the resin. . kwh/kg or lower when the specific energy is lower than 〇. 14 kWh/iro· 〇, Λ 1 single: the number of gels with a size of 3Q (four) in the vertical area can be reduced::::^ Film surface and surface ZD - The degree of gelation is evaluated as an advantage of optics, while the specific energy exceeds 〇14 kWh/kg, the excessive shear/force generated by the free radicals during partial degradation of the molecular bonds. Therefore, the formation and growth of the gel can be promoted. y should

脂環 200914255Grease ring 200914255

File:TW478!F 共聚合物樹脂接受 特疋月匕置,在64〇 _ 〇〇 或更大的 或更大尺寸的大凝膠數目為":::面積中具30 可由肉眼觀察到。此外,田:成或更多。此時,凝膠 膜的穿透性減少,因而逆成=勝,薄膜的霧性增加且薄 度。 ^成樹脂做為—光學薄膜的困難 用於製造本發明光學薄 環烯烴共聚合物樹脂,其令至小二右二,為使用-脂 稀烴單體,如降冰;^結構的脂環 稀共聚合。 降冰片烯何生物、或環戍烯與乙 聚合物樹脂具有比用於光學薄膜之其他 的透明度。脂環_共聚合物樹脂被認為是用於 ^子料的出色材料因其低吸濕性。商業上可取得的脂環 烯煙共聚合物樹脂包括Mitsui ehemieals ^生產的〈 APEL 及 Τιcona Corp,生產的 T〇pas。 a^述脂環烯烴共聚合物樹脂的產品形式不侷限本發 月範可1^ #知此技蟄者所已知。彳量抗熱性及薄膜的 可‘私丨生,I曰環烯煙共聚物樹脂的莫耳數中較佳含有8莫 耳%至16莫耳%的脂環單體。 在本文中,藉本發明適當實施例進一步描述本發明之 成份及功能,但是此些實施例並非以任何方式用以限制本 發明。未在本文中描述的内容可由熟於本發明相關技術人 士在無困難下瞭解’因此,且將省去其等之描述。 10 200914255File: TW478!F Copolymer resin is accepted for special months, and the number of large gels at 64 〇 _ or larger or larger is 30 in the "::: area visible to the naked eye. In addition, Tian: Cheng or more. At this time, the penetration of the gel film is reduced, so that the reverse is successful, and the haze of the film is increased and thin. The difficulty of forming a resin as an optical film is used to manufacture the optical thin ring olefin copolymer resin of the present invention, which is the second to the second, which is a alicyclic ring using a lipid-lowering monomer such as ice-reducing structure. Dilute copolymerization. The norbornene organism, or the cyclodecene and the ethylene polymer resin, has a higher transparency than that used for the optical film. The alicyclic-copolymer resin is considered to be an excellent material for the sub-material because of its low hygroscopicity. Commercially available alicyclic olefinic copolymer resins include T〇pas manufactured by APEL and Τιcona Corp., manufactured by Mitsui ehemieals. The product form of the alicyclic olefin copolymer resin is not limited to this one. It is known to those skilled in the art. The amount of the heat resistance and the film may be 'privately produced, and the number of moles of the I olefinic olefin copolymer resin preferably contains from 8 mol% to 16 mol% of the alicyclic monomer. In the present invention, the components and functions of the present invention are further described by the appropriate embodiments of the present invention, but such embodiments are not intended to limit the invention in any way. The content not described herein can be understood by those skilled in the art without difficulty, and thus the description thereof will be omitted. 10 200914255

File:TW4781F 實施例1File:TW4781F Example 1

蚀:衣造一光學脂環烯烴共聚合物薄膜。尤1, 3L的元全進料方法作為 J 機作為擠屋機,及薄膜系統。早螺桿擠璧 n i 衣以3又備的完整結構繪示於筮9 圖。树脂熔融物通過一 、 如第la圖所- i 在冷卻滾筒3上洗鑄。 (=A : 丁叹计螺桿為具有—壓縮比例為4 : 1 仏摅 為36。螺桿rpm設定在36rpm。其他條件 依據列於表1的製程條件μ '、牛 轉動馬達的安培數,及己錄在製程期間用於螺桿 苜。在外曾— ,、干馬達的工作電能依此記錄計 :預時擠㈣輸出後’其係藉測量由衝模在 工 作電处r :一 Η埜出之樹脂的擠壓機輸出,螺桿馬達的 作“除以母小時的擠壓機輸出以獲得特定能量。 最後通過冷却滾筒的具有100 _厚度的薄膜使用— 非接觸式照明計觀察64〇 、 # Φ ^ 1 n #mX48〇 面積。記錄在此面 積中存在的别10凝膠的平 大的凝膠數。 Ί尺寸及&寸為30 _或更 實施例2 計量:= ;光學脂環烯烴共聚合物薄膜。使用 =進^法作為樹脂供應系統,及設計供應比完全進料 表1的穿』程條株:V pm及其他條件依據列於 膠分柄= C 量的計算及在製成薄膜之凝 少 &相同於貫施例1的方法進行。 200914255Eclipse: A film of optical alicyclic olefin copolymer film. In particular, the 1,3L full-feed method is used as a J-machine as a squeezer and a film system. The early screw squeezing 璧 n i clothing is shown in Figure 筮9. The resin melt is washed on the cooling drum 3 by, for example, the first drawing. (=A: The singer screw has a compression ratio of 4:1 仏摅 is 36. The screw rpm is set at 36 rpm. Other conditions are based on the process conditions listed in Table 1 μ', the amperage of the cattle turning motor, and It is recorded during the process for the screw 苜. In the outside, the working energy of the dry motor, according to this record: pre-time squeeze (four) after the output 'the system is measured by the die at the working electricity r: a resin from the wilderness The output of the extruder, the screw motor is divided by the output of the extruder at the mother hour to obtain a specific energy. Finally, the film with a thickness of 100 _ through the cooling roller is used - a non-contact illuminometer to observe 64 〇, # Φ ^ 1 n #mX48〇 area. Record the number of gels of the other 10 gels present in this area. Ί Size and & inch 30 _ or more Example 2 Measure: = ; optical alicyclic olefin copolymer Film. Use the = method as the resin supply system, and the design supply is more than the complete feed table of the model: V pm and other conditions are based on the calculation of the rubber split handle = C and in the film The coagulation & is the same as the method of Example 1. 200914255

FiIe:TW4781F 實施例ί 於實= = = =稀烴共聚合物薄膜。以相同 低熔點的蠟盥樹脂、、曰人、,凡王退枓方法。 機之間的摩擦最小。佶 作匕 vr A ^ ^ 使用於本文的蠟為Henkel AG & Co KGaA 生產的 L〇xiol Ep_8fn。織从人 θ Lo· 61壤的含ι為〇. 4wt%。蟫椁 rpm及其他條件依據列於表1的製程條件妓。特定1干曰 的計算及在製成薄膜之、耗晚八k 寻疋此里 進行。 风㈣之鄉分析依相同於實施例1的方法 對照實施例1及2 桿轉動速度以造成特定能量超過在實施例中FiIe: TW4781F Example ί = = = = Thin hydrocarbon copolymer film. The same low melting point of waxy resin, scorpion, and the king of the method of withdrawal. The friction between the machines is minimal.佶 佶 匕 vr A ^ ^ The wax used in this paper is L〇xiol Ep_8fn produced by Henkel AG & Co KGaA. Weaving from human θ Lo· 61 soil contains ι 〇. 4wt%.蟫椁 rpm and other conditions are based on the process conditions listed in Table 1. The calculation of the specific 1 dry 及 is carried out in the production of a thin film. Wind (4) Hometown analysis is the same as the method of Example 1. Compare the rotation speeds of the Examples 1 and 2 to cause specific energy to exceed the embodiment.

2的㈣。❹㈣於實_ 1的方法以完全進料作為 統。螺# rPm及其他條件依據列於表1的製 =牛設定。特定能量的計算及在製成薄膜 相同於實施例1的方法進行。 刀析依 對照實施例3及4 一使用具有低壓縮比例的螺桿,但壓縮區段的長度與 =貫施例的相較為延長,故減少在壓縮間施用至樹脂的應 ’且因㈣成特定能量超過實施例巾計#的範圍。如 /圖所示’設計螺桿為具有2: 1 (=C: D)之壓縮比例及 /D為36。擠出溫度如實施例設定在26〇2(:及低於實施例 250-〇c。螺桿rpm及其他條件依據列於表1的製程條件 12 2009142552 (four). ❹ (4) The method of _ 1 is based on complete feeding. Snail # rPm and other conditions are based on the system listed in Table 1 = cattle setting. The calculation of the specific energy was carried out in the same manner as in Example 1 in the production of the film. According to Comparative Examples 3 and 4, a screw having a low compression ratio is used, but the length of the compression section is longer than that of the embodiment, so that the application to the resin during compression is reduced, and (four) is specific. The energy exceeds the range of the embodiment towel #. As shown in the figure, the design screw has a compression ratio of 2: 1 (=C: D) and /D is 36. The extrusion temperature was set to 26 〇 2 as in the examples (: and below Example 250-〇c. Screw rpm and other conditions are based on the process conditions listed in Table 1 12 200914255

FiIe:TW478!F 設定。特定能量 實施例1的方法=算及在製成薄膜之凝膠分析依相同於 於表 ,據實施例及對照實施狀製成_的擠出製程列FiIe: TW478!F setting. Specific energy The method of Example 1 = calculation and gel analysis of the film formed in the same manner as in the table, according to the examples and comparative examples of the extrusion process column

[表Π 樹脂供 應系統 ——-—„ 擠出 溫度 單位 - QC 實施例 1 完全 260 實施例 2 計量 260 實施例 3 完全 260 對照實 施例1 完全 260 對照實 施例2 完全 260 對照實 施例3 完全 260 對照實 施例4 完全 250 螺桿壓 縮比例[Table resin supply system - - „ extrusion temperature unit - QC Example 1 Complete 260 Example 2 Metering 260 Example 3 Complete 260 Comparative Example 1 Complete 260 Comparative Example 2 Complete 260 Comparative Example 3 Complete 260 Comparative Example 4 Full 250 screw compression ratio

擠壓機 螺桿 RPM電能Extruder screw RPM electric energy

輸出 Kg/hr 4Output Kg/hr 4

44

22

44

44

22

14 4.〇5 18.014 4.〇5 18.0

13 20091425513 200914255

File:TW478IF 能量t㈣件㈣融擠壓物質而製成之薄膜的特定 1 〇凝膠的平j勺尺+ gβ 位面積具有尺^尺寸及在640㈣X彻Ρ單File: TW478IF energy t (four) pieces (four) specific film made by extruding material 1 〇 gel flat j spoon + gβ bit area with ruler size and in 640 (four) X thoroughly

Jam或更大的凝膠數為列於表2中。 ,ΙΑΙΙThe number of gels of Jam or larger is listed in Table 2. , ΙΑΙΙ

非常=顯讀本發明製造之_的崎尺寸及數目A 戸常有關於特定能量。 目為 rpm 貝施例1在〇. 14 kWh/kg或更低的特定能旦 口本發明目的。另-方面’對照實施例1及2降:螺以符 14 200914255Very = significant reading of the size and number of sag produced by the invention A 戸 is often related to a specific energy. The purpose of the present invention is to rpm a specific energy of Example 1 at 14 kWh/kg or less. Another-aspect 'Comparative Examples 1 and 2 fall: Snails 14 200914255

File:TW4781F 以控制特定能量至超過在實施例中計算的範圍。因此,實 施例1具有一平均凝膠尺寸約20%或更小於對照實施例i 及2者。而且,其觀察到在實施例丨中具有3〇 或更 大尺寸之凝膠數明顯降至1,其與對照實施例丨及2相比 分別為3及3. 5。 對照實施例2及實施例2具有相同的製程條件,除了 樹脂供應线不同。實㈣2藉由在龍機内輯量進料 增加空隙空間而減少摩擦以降低特定能量。因此,以降低 特定能量的實施例2形成具降低20%之凝膠平均尺寸的凝 膠。此外’具有30 //m或更大尺寸之凝膠數為〇 8,其相 似於貫施例1。 對照實施例3及4使用改良之螺桿,其降低螺桿壓縮 比,以降低壓縮製程期間施加在樹脂的摩擦力。然而,對 照實施例3及4顯示高特定能量,其係因為由壓縮區段的 延長而引起摩擦產生區段的延長。在對照實施例…File: TW4781F to control specific energy to exceed the range calculated in the examples. Thus, Example 1 has an average gel size of about 20% or less than that of Comparative Examples i and 2. Further, it was observed that the number of gels having a size of 3 Å or more in the Example 明显 was significantly reduced to 1, which was 3 and 3.5, respectively, compared with the Comparative Examples 丨 and 2. Comparative Example 2 and Example 2 had the same process conditions except that the resin supply lines were different. Real (4) 2 reduce the friction to reduce the specific energy by increasing the void space in the dragon machine. Therefore, Example 2, which lowers the specific energy, forms a gel having an average gel size which is reduced by 20%. Further, the number of gels having a size of 30 // m or more is 〇 8, which is similar to that of Example 1. Comparative Examples 3 and 4 used a modified screw which reduced the screw compression ratio to reduce the friction applied to the resin during the compression process. However, Comparative Examples 3 and 4 show a high specific energy due to the extension of the friction generating section due to the elongation of the compression section. In the comparative example...

中,具有30 /zm或更大尺寸之凝膠數與對照實施例!及2 ==低至某?範圍。然而,由於低壓縮比例,紀錄到的 ’夕是2或更多。而且’平均凝膠尺寸沒有改變。 在實施例3中,加人蠘至擠_中以減少 的摩擦,特定能量·地降低即使其他條件相同内 要:·'、、貫環。因此,由實施例3及對照實施例3的社 低至約m ’且依在特定能量的降 "有30以"1或更大尺寸之凝膠數由2降至0.8。 上述結果顯示,不論在產生薄膜及製程條件如螺桿設 200914255In the case of a gel having a size of 30 /zm or larger and a comparative example! And 2 == low to some? range. However, due to the low compression ratio, the recorded eve is 2 or more. Moreover, the average gel size did not change. In the third embodiment, the entanglement is added to the squeezing _ to reduce the friction, and the specific energy and the ground are lowered even if other conditions are the same: · ', , and the ring. Therefore, the decrease of the specific energy by the embodiment 3 and the control example 3 is as low as about m' and the number of gels having a size of "1 or more is reduced from 2 to 0.8. The above results show that regardless of the film and process conditions such as screw set 200914255

File:TW4781F 二桿旋轉速度、及其類似的設傷結構改變, 骖形成傾向與特定能量有密切的闕係。 看到,經由降低特定能量製成的脂環稀烴 ㈣’其做為一製程參數,具有抑制凝璆形成及 此,可易於使用脂環稀烴共聚合物相做為一呈 有出色表面特性的光學薄膜。即,本發明之光學薄ς 脂擠出製㈣卩相為大量抑制凝料成及成長,*具有2 霧度及高光穿透性。因此,本發明之光學薄膜ς用 於製造顯示產品如LCD。 雖然本發明較佳實施例因說明目的而描述,熟於是 項技術人士可瞭解在未偏離本發明範疇及精神,如本案 申請專利範圍中界定者’不同修飾、加餘取代作用為 可行的。 200914255File: TW4781F Two-bar rotation speed, and its similar damage structure change, the tendency of 骖 formation is closely related to specific energy. It can be seen that the alicyclic hydrocarbon (4) produced by lowering the specific energy is used as a process parameter to inhibit the formation of condensate and thus, the alicyclic hydrocarbon copolymer phase can be easily used as an excellent surface characteristic. Optical film. That is, the optical thin resin extruded according to the present invention (4) has a large amount of ruthenium phase and inhibits the formation and growth of the aggregate, and has 2 haze and high light transmittance. Therefore, the optical film of the present invention is used for the manufacture of display products such as LCDs. While the preferred embodiment of the present invention has been described by way of illustration, it will be appreciated by those skilled in the art that the various modifications and additions are possible without departing from the scope and spirit of the invention, as defined in the scope of the patent application. 200914255

File:TW478IFFile:TW478IF

f圖式簡單說明J 第〗a圖為說明依據本發明之— 縮比例的螺桿圖示;—十之具有 第1 b圖為說明依據本發明 ^ 9 . , . „ _ 明之一貧施例所設計之且有 2. U/C: D)l縮比例的螺桿圖示;及 、有BRIEF DESCRIPTION OF THE DRAWINGS Fig. a is a diagram showing a screw scale according to the present invention; Fig. 1b is a diagram showing the first embodiment of Fig. 1 and Fig. Designed with 2. U/C: D) l scaled screw diagram;

第2 ®為-說明本發明之施則㈣ 程之設備的簡單示意圖。 4出I 主要元件符號說明 17The second ® is a simple schematic diagram illustrating the apparatus of the fourth embodiment of the present invention. 4 out I main component symbol description 17

Claims (1)

200914255 File:TW4781F 十、申請專利範圍: 種光车溥膜,其由脂環烯烴共聚合物製成,其中 該溥膜在640 /, m ν β。。 ,.$ ^ “mx 480以m單位面積具有尺寸為⑽//m 或更大的凝膠數為小於15。 .申叫專利範圍第1項所述之薄膜,其中該薄膜 480 單位面積中存有具30 或更大 尺寸的凝膠數為少於12。 & ('嫌炉丑專利範圍第1項所述之薄膜’其中該脂環 形^白^月曰^错由共聚合至少—脂環稀烴單體與乙稀而 烯烴ΚΙ、::利範圍第3項所述之薄膜,其中該脂環 Μ早體為選自降冰片稀 與其等之組合所組成的組群。片婦何生物、及%戍蝉 5.如申請專利範圍第3項所述之 豆 烯烴單體為樹脂莫耳數 /帛…、^月曰衩 夭吁数芡《莫耳%至16莫耳%量。 I· ·—種製造如申請專利笳Ifl楚1 膜的方法,其包含在卜W圍第1項所述之光學薄 或更低值的特定能量擠廢脂環2;;:0·二:kg 量為在擠壓機一中螺桿轉動之1、^物’其_中特定能 撥壓機輸出。 电此除以母小時的 7·如申請專利範圍第6項所述之 烯烴共聚物以〇. u kWh/k / ,/、中该脂環 8·如申請專利範圍第 烯烛共聚物為經由共聚合至少=方法’其中該月旨環 月曰裱烯烴單體與乙烯而 200914255 hiIe;JW47«IF 獲得之樹脂。 9.如申請專利範圍帛δ 婦煙早體該脂料烴單體為 叹方法,其中該脂環 生物、及環戊稀愈立条冰片烯、降冰片烯衍 〗。.如申請專利=::r组群。 環馳單體為樹脂料數之其量中㈣200914255 File: TW4781F X. Patent application scope: The ruthenium film is made of alicyclic olefin copolymer, wherein the ruthenium film is 640 /, m ν β. . , .$ ^ "mx 480 has a gel number of (10) / / m or more in units of m per unit of less than 15. The film of claim 1 wherein the film is stored in 480 unit area The number of gels having a size of 30 or more is less than 12. & ('The film described in the first item of the ugly patent range> wherein the fat ring is white ^ ^ 曰 ^ wrong by copolymerization at least - fat The invention relates to the film of the third aspect of the invention, wherein the alicyclic sputum precursor is a group selected from the group consisting of norbornene and the like. Biological, and % 戍蝉 5. The bean olefin monomer as described in claim 3 is a resin mole number / 帛 ..., ^ 曰衩夭 曰衩夭 芡 "Mor% to 16% by volume. I. A method of manufacturing a film as claimed in the patent 笳Ifl Chu 1 , which comprises an optical thin or lower specific energy squeezing alicyclic ring 2 as described in item 1 of the wei W;;: 0·2: The amount of kg is the output of the specific energy of the screw in the extruder 1 . The electric energy is divided by the mother hour. 7. The olefin as described in claim 6 The polymer is 〇.u kWh/k / , /, the alicyclic ring 8 · as claimed in the patent range, the ene candle copolymer is via copolymerization at least = method 'where the month is the ring olefin monomer and ethylene 200914255 hiIe; JW47 «IF obtained resin. 9. If the patent application scope 帛 δ 妇 烟 early body of the fat hydrocarbon monomer sigh method, the alicyclic organism, and cyclopentane erectane borneol, norbornene烯 衍.. If applying for a patent =::r group. The ringing monomer is the amount of resin material (4)
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JP6113683B2 (en) * 2014-03-25 2017-04-12 富士フイルム株式会社 Transparent film and manufacturing method thereof, laminated film, transparent conductive film, hard coat film, touch panel, polarizing plate and display device

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JP2006142715A (en) * 2004-11-22 2006-06-08 Sekisui Chem Co Ltd Manufacturing method of molding
JP4704896B2 (en) * 2005-11-25 2011-06-22 積水化学工業株式会社 Manufacturing method of optical film

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CN102958669A (en) * 2010-06-25 2013-03-06 宝理塑料株式会社 Method for producing molded article
CN113518938A (en) * 2019-02-28 2021-10-19 日东电工株式会社 Optical laminate

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