TW201105480A - Method for producing optical film, optical film, and apparatus for producing optical film - Google Patents

Method for producing optical film, optical film, and apparatus for producing optical film Download PDF

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Publication number
TW201105480A
TW201105480A TW099107613A TW99107613A TW201105480A TW 201105480 A TW201105480 A TW 201105480A TW 099107613 A TW099107613 A TW 099107613A TW 99107613 A TW99107613 A TW 99107613A TW 201105480 A TW201105480 A TW 201105480A
Authority
TW
Taiwan
Prior art keywords
film
optical film
producing
rolling
melt
Prior art date
Application number
TW099107613A
Other languages
Chinese (zh)
Other versions
TWI522225B (en
Inventor
Yasutoshi Ito
Original Assignee
Konica Minolta Opto Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Konica Minolta Opto Inc filed Critical Konica Minolta Opto Inc
Publication of TW201105480A publication Critical patent/TW201105480A/en
Application granted granted Critical
Publication of TWI522225B publication Critical patent/TWI522225B/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C33/00Moulds or cores; Details thereof or accessories therefor
    • B29C33/56Coatings, e.g. enameled or galvanised; Releasing, lubricating or separating agents
    • B29C33/60Releasing, lubricating or separating agents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C33/00Moulds or cores; Details thereof or accessories therefor
    • B29C33/56Coatings, e.g. enameled or galvanised; Releasing, lubricating or separating agents
    • B29C33/58Applying the releasing agents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C33/00Moulds or cores; Details thereof or accessories therefor
    • B29C33/56Coatings, e.g. enameled or galvanised; Releasing, lubricating or separating agents
    • B29C33/60Releasing, lubricating or separating agents
    • B29C33/62Releasing, lubricating or separating agents based on polymers or oligomers
    • B29C33/64Silicone
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C43/00Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
    • B29C43/22Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor of articles of indefinite length
    • B29C43/30Making multilayered or multicoloured articles
    • B29C43/305Making multilayered articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/07Flat, e.g. panels
    • B29C48/08Flat, e.g. panels flexible, e.g. films
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9135Cooling of flat articles, e.g. using specially adapted supporting means
    • B29C48/915Cooling of flat articles, e.g. using specially adapted supporting means with means for improving the adhesion to the supporting means
    • B29C48/9155Pressure rollers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/02Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
    • B29C55/10Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial
    • B29C55/12Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial
    • B29C55/14Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial successively
    • B29C55/143Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets multiaxial biaxial successively firstly parallel to the direction of feed and then transversely thereto
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9135Cooling of flat articles, e.g. using specially adapted supporting means
    • B29C48/914Cooling of flat articles, e.g. using specially adapted supporting means cooling drums
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2001/00Use of cellulose, modified cellulose or cellulose derivatives, e.g. viscose, as moulding material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2007/00Flat articles, e.g. films or sheets

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Moulding By Coating Moulds (AREA)
  • Moulds For Moulding Plastics Or The Like (AREA)

Abstract

Disclosed are: a method for producing an optical film in which the release properties of a thermoplastic resin film from a touch roller is improved and transverse irregularities are not caused; an optical film produced by the production method; and an apparatus for producing an optical film. The method for producing an optical film comprises a casting step in which a molten material containing a thermoplastic resin is extruded into a film shape on the surface of a rotary support from a casting die; and a sandwiching and pressing step in which the film-shaped molten material extruded in the casting step is sandwiched and pressed between the rotary support and a sandwiching and pressing rotator. In the production method, in order to improve release properties between the sandwiching and pressing rotator and the film-shaped molten material, a release property adjusting agent is applied to the surface of the sandwiching and pressing rotator.

Description

201105480 六、發明說明: 【發明所屬之技術領域】 本發明係關於以溶融流延成膜法製造含有纖維素樹脂 等之熱可塑性樹脂的光學薄膜用的光學薄膜之製造方法、 製造裝置及光學薄膜。 【先前技術】 液晶顯示裝置相較於以往的CRT顯示裝置,因較省 空間、省能源,因此廣泛的作爲監視器使用。進一步普及 作爲電視上使用。這種液晶顯示裝置中使用偏光板用之保 護薄膜或相位差薄膜等各種光學薄膜。 偏光板用之保護薄膜係貼附於由延伸聚乙烯醇所構成 之偏光薄膜上,保護偏光薄膜用的薄膜,使用含有纖維素 樹脂等之熱可塑性樹脂的薄膜。相位差薄膜係用於爲了擴 大視角或提高對比等者,將含有纖維素樹脂等之熱可塑性 樹脂的薄膜進行延伸等,賦予延遲(retardation )者。有 時稱爲光學補償薄膜。 這種光學薄膜之製造方法可分爲溶融流延成膜法與溶 液流延成膜法。前者係將熱可塑性樹脂經加熱溶融後的熔 融物流延於支持體上,冷卻固化後,必要時可進行延伸等 形成薄膜的方法,後者係將聚合物溶解於溶劑,將該溶液 流延至支持體上,溶劑蒸發後,必要時可進行延伸等形成 薄膜的方法。 以往,因爲膜厚之均一化容易等的理由’因此藉由溶[Technical Field] The present invention relates to a method for producing an optical film for producing an optical film containing a thermoplastic resin such as a cellulose resin by a melt casting film formation method, a manufacturing apparatus, and an optical film. . [Prior Art] Compared with the conventional CRT display device, the liquid crystal display device is widely used as a monitor because it is space-saving and energy-saving. Further popularization as used on television. In such a liquid crystal display device, various optical films such as a protective film for a polarizing plate or a retardation film are used. The protective film for a polarizing plate is attached to a polarizing film made of a stretched polyvinyl alcohol to protect a film for a polarizing film, and a film containing a thermoplastic resin such as a cellulose resin is used. The retardation film is used to extend a film or the like of a thermoplastic resin such as a cellulose resin to provide a retardation. Sometimes referred to as an optical compensation film. The method for producing such an optical film can be classified into a melt casting film forming method and a solution casting film forming method. The former is a method in which a molten stream obtained by heating and melting a thermoplastic resin is extended on a support, and after cooling and solidifying, a film can be formed by stretching or the like if necessary, and the latter is obtained by dissolving the polymer in a solvent and casting the solution to a support. After the solvent is evaporated, a method of forming a film such as stretching may be carried out if necessary. In the past, the reason for the uniformity of the film thickness is easy, etc.

E -5- 201105480 液流延成膜法之製造爲主流。但是溶液流延成膜法係因溶 劑回收,需要巨大的生產設備等的問題,因而藉由無此等 問題之融流延成膜法製造光學薄膜受到矚目。 此等光學薄膜要求光學的性能、特別是延遲均一。隨 著監視器或TV之大型化或輕量化,延遲之均一性要求越 來越嚴格,同時也強烈要求光學薄膜之廣寬化、薄膜化、 表面平滑性。 藉由溶融流延成膜法製造光學薄膜一般係將含有纖維 素樹脂等之熱可塑性樹脂的熔融物由流延模擠出成薄膜狀 於旋轉支持體(以下也稱爲鑄造輥(cast roll))的表面 ,擠出後之薄膜狀之熔融物(以下也稱爲薄膜)藉由旋轉 支持體與挾壓旋轉體(以下也稱爲接觸輥(touch roll ) )挾壓得到薄膜。接觸輥的表面爲了提高薄膜之表面平滑 性,而施加鏡面加工。 進行此挾壓時,施加於薄膜的壓力會影響樹脂的配向 狀態,所得之薄膜的延遲會變化,因此爲了得到延遲均一 性高的光學薄膜時,以充分均一壓力挾壓是很重要的。 但是隨著光學薄膜之廣寬化,流延模之寬度變寬,被 擠出之薄膜狀之熔融物藉由鑄造輥與接觸輥以均一壓力挾 壓有困難。 解決此種問題點的方法例如接觸輥使用外周具有金屬 圓筒之彈性輥(以下也稱爲彈性金屬輥),使挾壓時之壓 力均一的方法或專利文獻1提案將由流延模流至鑄造輥之 熔融物的溫度設定爲高於以往,即使鑄造輥與接觸輥之挾 201105480 壓力多少不均一,也可抑制延遲不均的方法。 [先行技術文獻] [專利文獻] [專利文獻1]特開2005- 1 72940號公報 【發明內容】 [發明槪要] [發明欲解決的課題] 但是被擠壓至鑄造輥上之含有熱可塑性樹脂之熔融物 與表面經鏡面加工之接觸輥接觸加壓時,容易產生由接觸 輥之薄膜剝離的不良情形,有時薄膜寬度方向會產生條紋 狀之不均(橫向不均)。此外,接觸輥使用彈性金屬輥或 如專利文獻1 ’將熔融物之溫度昇高設定時,對接觸輥之 附著力變大,有時產生剝離不良,更容易產生橫向不均, 且延遲不均也變大的問題。 因此’本發明之目的係提供提高接觸輥之薄膜的脫模 性’不會產生橫向不均或延遲不均之光學薄膜之製造方法 、光學薄膜之製造裝置及以該製造方法製造的光學薄膜。 [解決課題的手段] 爲了解決上述課題,本發明係具有以下的特徵者。 1. 一種光學薄膜之製造方法,其係具備將含有熱可 塑性樹脂之熔融物由流延模擠出成薄膜狀於旋轉支持體表 201105480 面的流延步驟、 將前述流延步驟擠出之薄膜狀的熔融物以前述旋轉支 持體與挾壓旋轉體進行挾壓之挾壓步驟的光學薄膜之製造 方法, 其特徵係在前述挾壓旋轉體表面塗佈使前述挾壓旋轉 體與前述薄膜狀之熔融物之脫模性良好的脫模性調整劑。 2-如前述第1項之光學薄膜之製造方法,其中前述 脫模性調整劑含有與前述熔融物所含之添加劑中至少1種 相同的材料。 3.如前述第1或2項之光學薄膜之製造方法,其中 前述脫模性調整劑爲在前述光學薄膜之內部用於吸收紫外 線的紫外線吸收劑。 4·如前述第1〜3項中任一項之光學薄膜之製造方法 ,其中前述脫模性調整劑之沸點爲1 5 0~ 2 5 0。(:。 5. 如前述第1~4項中任一項之光學薄膜之製造方法 ,其中塗佈前述脫模性調整劑之厚度爲0.05〜lOOOym。 6. 如前述第1〜5項中任一項之光學薄膜之製造方法 ,其中則述旋轉支持體表面與水的接觸角S1與塗佈前述 脫模性調整劑後之挾壓旋轉'體表面與水之接觸角S 2爲 0.5°<S2-S1<100°的關係。 7. 如前述第1~6項中任一項之光學薄膜之製造方法 ’其中前述挾壓旋轉體按壓於前述旋轉支持體之狀態之前 述薄膜狀之熔融物的搬送張力T1與前述挾壓旋轉體未按 壓於前述旋轉支持體之狀態之前述薄膜狀之熔融物的搬送 -8 - 201105480 張力T2之差T1-T2爲1〜250N。 8. 如前述第1〜7項中任一項之光學薄膜之製造方法 ,其中前述熱可塑性樹脂爲纖維素酯系樹脂。 9. 一種光學薄膜,其特徵係藉由前述第1~8項中任 一項之光學薄膜之製造方法所製造者。 10. —種光學薄膜之製造裝置,其係具有: 將含有熱可塑性樹脂之熔融物擠出成薄膜狀於旋轉支 持體表面的流延模、 將前述流延模擠出之薄膜狀的熔融物以前述旋轉支持 體與挾壓旋轉體進行挾壓之挾壓手段的光學薄膜之製造裝 置,其特徵係具有在前述挾壓旋轉體表面塗佈使前述挾壓 旋轉體與前述薄膜狀之熔融物之脫模性良好的脫模性調整 劑之脫模性調整劑塗佈裝置。 發明效果 依據本發明時,將脫模性調整劑塗佈於挾壓旋轉體的 表面後,以旋轉支持體與挾壓旋轉體挾壓薄膜狀之熔融物 ,因此提高挾壓旋轉體之薄膜的脫模性。因此,可提供薄 膜由挾壓旋轉體剝離時,不會產生橫向不均或延遲不均之 光學薄膜之製造方法、光學薄膜之製造裝置及以該製造方 法製造的光學薄膜。 [實施發明之形態] 以下參照圖面說明實施本發明的形態,但是本發明不 -9 - 201105480 受此限制。 本發明之光學薄膜之製造方法係具備將含有熱可塑性 樹脂之熔融物由流延模擠出成薄膜狀於旋轉支持體(鑄造 輥)表面的流延步驟、 將前述流延步驟擠出之薄膜狀的熔融物以旋轉支持體 與挾壓旋轉體(接觸輥)進行挾壓之挾壓步驟的光學薄膜 之製造方法, 其特徵係在前述挾壓旋轉體表面塗佈使前述挾壓旋轉 體與前述薄膜狀之熔融物之脫模性良好的脫模性調整劑之 光學薄膜之製造方法β 圖1係表示使用本發明之光學薄膜之製造方法之一實 施形態之製造裝置的流延步驟與挾壓步驟的槪略圖。流延 步驟係由作爲流延手段之流延模4將含有熱可塑性樹脂之 熔融物Υ擠出於鑄造輥5上之Ρ1的位置。此時接觸輥6 的表面,比挾壓部Ρ2之位置更上流側,藉由脫模性調整 劑塗佈裝置1 〇〇被塗佈脫模性調整劑1 04。由流延模4被 擠出至鑄造輥5上之Ρ1位置的熔融物Υ係藉由挾壓步驟 在Ρ2位置以挾壓手段之接觸輥6與鑄造輥5挾壓。被挾 壓之熔融物成爲薄膜狀,被搬送至鑄造輥5上,在Ρ3位 置剝離,然後移至下一步驟。 脫模性調整劑塗佈裝置1 00係以吸取輥1 02吸取被加 溫至所定溫度之貯存槽105內之液狀脫模性調整劑1 04, 藉由限制刮板1 03限定爲一定量,限定後之吸取輥1 〇 2上 之脫模性調整劑104轉移至塗佈輥101,塗佈於接觸輥6 -10- 201105480 上之構成所成。 如上述,挾壓步驟之前,在接觸輥6表面塗佈脫模性 調整劑後,在挾壓步驟藉由鑄造輥5與接觸輥6挾壓薄膜 ,因此薄膜與鑄造輥5之黏著力大於薄膜與接觸輥6之黏 著力,可抑制接觸輥6與薄膜在剝離時產生剝離不良。特 別是爲了提高薄膜表面之平滑性,對接觸輥6表面進行鏡 面加工時或接觸輥使用彈性金屬輥時,爲了使挾壓步驟無 按壓不均,降#殘留相位差,而使薄膜溫度成爲高溫進行 挾壓時等,容易產生接觸輥與薄膜之剝離不良,但是藉由 本發明可有效稍除剝離不良。 上述構成倡係對接觸輥6塗佈脫模性調整劑,但是在 接觸輥6與鑄造輥5之兩方表面也可塗佈脫模性調整劑, 調整爲薄膜與鑄造輥5之黏著力大於薄膜與接觸輥6之黏 著力’可抑制接觸輥6與薄膜在剝離時產生剝離不良即可 〇 本發明之脫模性調整劑只要是提高接觸輥6與薄膜之 脫模性的材料畤,即無特別限定,可爲液體狀或固體狀, 製品較佳爲不會影響必要之光學薄膜特性者。更佳爲與光 學薄膜所用之添加劑相同的材料作爲脫模性調整劑使用。 使用與這種添加劑相同材料的脫模性調整劑時,即使塗佈 於接觸輥6之脫模性調整劑附著於光學薄膜之表面,也幾 乎不會影響光學薄膜特性,且可有效的消除接觸輥6與薄 膜之剝離不良。 脫模性調整劑之具體例有聚矽氧油或二甲基矽氧烷、 I S] -11 - 201105480 二氯甲烷、作爲光學薄膜之添加劑使用之可塑劑、紫外線 吸收劑等。此外,也可使用分散有有機或無機微粒子的液 狀者。 脫模性調整劑之弗點較佳爲150〜250°C。沸點爲此範 圍時’在接觸輥6表面係接觸輥之表面溫度低於150。, 因此脫模性調整劑成爲液狀或固體狀,發揮脫模性調整劑 的功能’轉移至由接觸輥6脫模後之薄膜表面的脫模性調 整劑係在其後之延伸步驟等高溫的步驟,設定爲沸點以上 可產生揮發,脫模性調整劑不會殘留於薄膜表面,可維持 光學薄膜的性能,故較佳。 脫模性調整劑特佳爲紫外線吸收劑。紫外線吸收劑係 剝離性高’而且以較薄的層可發揮脫模性,因此由接觸輥 6脫模後之薄膜表面的平滑性升高,故較佳。此外,原本 添加於光學薄膜使用之光學薄膜的構成材料,因此在製造 步驟中,即使混入光學薄膜內,也不會影響光學薄膜特性 ,故較佳。 塗佈於接觸輥表面之脫模性調整劑的塗佈膜厚較佳爲 0.05~1000/zm。設定爲此範圍的塗佈膜厚時,因塗佈太少 產生塗佈不良或因太厚使脫模性調整劑滯留於接觸輥與冷 卻輥之間,產生薄膜之橫向不均或延遲不均的危險性較少 ,故較佳。 鑄造輥5之表面Μ水之接觸角S1與塗佈脫模性調整 劑後之接觸輥6表面與水之接觸角S2爲0.5°<S2_S1<100° 的關係較佳。S 2-S 1設定爲此範圍,可減少產生脫模性調 -12- 201105480 整劑之塗佈不良(〇.5°以下)、脫模性調整劑之塗佈不均 成爲薄膜膜厚不均(1〇〇°以上)的危險性,故較佳。 輕表面與水之接觸角的測定係使用全自動接觸角計r CA-W型roll特型」(協和界面科學公司製)在23 °C、50 % RH之環境下測定對純水的接觸角。爲了兼顧純水蒸發 之測定値的變化與測定之安定性時,由純水滴滴下後5秒 至3 0秒以內結束測定。測定係藉由從連接液滴之左右端 點與頂點之直線之對固體表面之角度求得接觸角的0 /2法 。對於輥之軸方向由直角方向測定,滴下量設定爲70^1 〇 測定處係測定輥之中央部、左右端部5 cm之位置之3 處,各自圓周方向各90°之4處合計12處,以此平均値作 爲接觸角。 將接觸輥6按壓於鑄造輥5之狀態下之薄膜狀之熔融 物的搬送張力爲T 1、未將接觸輥6按壓於鑄造輥5之狀 態下之薄膜狀之熔融物的搬送張力T2時之T1-T2的値較 佳爲1 ~2 5 0N。搬送張力之測定係在鑄造輥5之下流側之 最近的輥之軸兩端分別安裝秤取鉛直方向之荷重的荷重計 ,計算將接觸輥6按壓或未按壓於鑄造輥5時之各自之荷 重計之差,該合計的値爲ΤΙ-Τ'2之値。 搬送張力之差之Τ1-Τ2的値設定在上述範圍時,由接 觸輥6剝離時之薄膜(某程度固化後之薄膜狀的熔融物) 無偏差(均勻),且無拉伸過度’因此不會因偏差造成之 膜厚不均或拉伸過度造成斷裂等,可安定般送由接觸輥6E -5- 201105480 The manufacture of the liquid casting film forming method is the mainstream. However, since the solution casting film forming method requires a large production facility due to the solvent recovery, it has been attracting attention by the melt casting film forming method without such a problem. These optical films require optical properties, particularly delay uniformity. With the increase in size or weight of monitors or TVs, the uniformity of delay is becoming more stringent, and the widening, thinning, and smoothness of optical films are strongly demanded. The optical film produced by the melt-casting film formation method is generally obtained by extruding a melt of a thermoplastic resin containing a cellulose resin or the like into a film shape on a rotary support by a casting die (hereinafter also referred to as a cast roll). The surface of the film-like melt (hereinafter also referred to as a film) after extrusion is pressed by a rotary support and a rolling rotating body (hereinafter also referred to as a touch roll) to obtain a film. The surface of the contact roller is mirror-finished in order to improve the surface smoothness of the film. When this rolling is performed, the pressure applied to the film affects the alignment state of the resin, and the retardation of the obtained film changes. Therefore, in order to obtain an optical film having high retardation uniformity, it is important to press at a sufficiently uniform pressure. However, as the width of the optical film is widened, the width of the casting die is widened, and the melted film-like melt is difficult to be uniformly pressed by the casting roll and the contact roll. A method for solving such a problem, for example, a method in which a contact roller uses an elastic roller having a metal cylinder on the outer circumference (hereinafter also referred to as an elastic metal roller) to make the pressure at the time of rolling uniform, or Patent Document 1 proposes to flow from a casting die to casting. The temperature of the melt of the roll is set higher than the conventional one, and even if the pressure of the casting roll and the contact roll is not uniform, the method of suppressing the unevenness of the delay can be suppressed. [PRIOR ART DOCUMENT] [Patent Document 1] [Patent Document 1] Japanese Laid-Open Patent Publication No. 2005- 1 72940 [Summary of the Invention] [Problem to be Solved by the Invention] However, the thermoplasticity contained in the casting roll is contained. When the melt of the resin is pressed and brought into contact with the surface-finished contact roll, the film of the contact roll is liable to be peeled off, and unevenness (lateral unevenness) may occur in the film width direction. Further, when the contact roller is an elastic metal roller or when the temperature of the melt is raised as in Patent Document 1, the adhesion to the contact roller is increased, and peeling failure may occur, and lateral unevenness is more likely to occur, and unevenness is uneven. It also becomes a big problem. Therefore, the object of the present invention is to provide a method for producing an optical film which does not cause lateral unevenness or unevenness in retardation, and a method for producing an optical film, and an optical film produced by the method. [Means for Solving the Problem] In order to solve the above problems, the present invention has the following features. A method for producing an optical film, comprising: a casting step of extruding a melt containing a thermoplastic resin into a film form on a surface of a rotating support sheet 201105480; and extruding the casting step The method for producing an optical film in which the molten material is subjected to a rolling step of rolling the rotating support and the rolling rotating body, wherein the rolling rotating body is coated with the rolling rotating body and the film. A mold release property adjuster having a good mold release property. The method for producing an optical film according to the above aspect, wherein the release property adjuster contains at least one of the same as the additive contained in the melt. 3. The method for producing an optical film according to the above item 1 or 2, wherein the release property adjusting agent is an ultraviolet absorber for absorbing ultraviolet rays inside the optical film. The method for producing an optical film according to any one of the items 1 to 3, wherein the release property adjuster has a boiling point of from 150 to 250. The method for producing an optical film according to any one of the above items 1 to 4, wherein the thickness of the release mold adjusting agent is from 0.05 to 100 μm. A method for producing an optical film, wherein a contact angle S1 between a surface of the rotary support and water and a contact angle S 2 of the surface of the rotating body after applying the release modifier are 0.5° < 7. The method of producing an optical film according to any one of the above-mentioned items 1 to 6, wherein the film-like melting of the rolling rotating body in a state of being pressed against the rotating support The difference T1 - T2 between the transport tension T1 of the object and the transport of the film-like melt in the state in which the rolling rotor is not pressed against the rotary support is -1 to 250N. The method of producing an optical film according to any one of the items 1 to 7, wherein the thermoplastic resin is a cellulose ester resin. 9. An optical film characterized by the optical according to any one of items 1 to 8. Manufacturer of the manufacturing method of the film. 10. Manufacturing of optical film Further, the method further comprises: casting a melt containing a thermoplastic resin into a film-forming casting die on a surface of a rotating support; and extruding the film-shaped melt extruded from the casting die by the rotating support and rolling The apparatus for producing an optical film of a rolling apparatus for pressing a body has a mold release property of applying a mold release property to the surface of the rolling rotating body to improve the mold release property of the rolling rotating body and the film-shaped melt. According to the present invention, the release property adjuster is applied to the surface of the rolling rotating body, and then the film is formed by rotating the support and the rolling rotating body. The melt is thus improved in the release property of the film of the rolling rotating body. Therefore, it is possible to provide a method for producing an optical film which does not cause lateral unevenness or uneven retardation when the film is peeled off from the rolling rotating body, and the production of the optical film. The apparatus and the optical film manufactured by the manufacturing method. [Embodiment of the invention] Hereinafter, the embodiment of the invention will be described with reference to the drawings, but the invention is not limited to -9 - 201105480. The method for producing an optical film according to the invention includes a casting step of extruding a melt containing a thermoplastic resin into a film form on a surface of a rotary support (casting roll), and extruding the casting step. a method for producing an optical film in which a molten material is subjected to a rolling step of rolling a rotating body and a rolling rotating body (contact roll), characterized in that the surface of the rolling rotating body is coated with the rolling rotating body and the foregoing Method for producing an optical film of a release property adjusting agent having a good mold release property as a film-like melt. FIG. 1 is a view showing a casting step and rolling of a manufacturing apparatus using an embodiment of the method for producing an optical film of the present invention. A step of the step of casting the melt containing the thermoplastic resin to the position of the crucible 1 on the casting roll 5 by the casting die 4 as a casting means. At this time, the surface of the touch roll 6 is moved upward from the position of the pressing portion ,2, and the release property adjusting agent 104 is applied by the release-adjusting agent applying device 1 。. The melt enthalpy which is extruded from the casting die 4 to the nip 1 position on the casting roll 5 is pressed by the contact roll 6 and the casting roll 5 at the Ρ 2 position by the pressing means at the Ρ 2 position. The melted product is formed into a film shape, conveyed to the casting roll 5, peeled off at the Ρ3 position, and then moved to the next step. The release-adjusting agent coating device 100 is configured to suck the liquid release-reducing agent 104 in the storage tank 105 heated to a predetermined temperature by the suction roller 102, and is limited to a certain amount by the restriction blade 103. The release-adjusting agent 104 on the selected suction roll 1 〇2 is transferred to the coating roll 101 and applied to the contact roll 6-10-201105480. As described above, before the rolling step, after the release agent is applied to the surface of the touch roll 6, the film is pressed by the casting roll 5 and the contact roll 6 in the rolling step, so that the adhesion of the film to the casting roll 5 is greater than that of the film. The adhesion to the contact roller 6 can suppress the occurrence of peeling failure of the contact roller 6 and the film at the time of peeling. In particular, in order to improve the smoothness of the surface of the film, when the surface of the touch roll 6 is mirror-finished or when the elastic metal roll is used for the contact roll, in order to prevent the pressing step from being uneven, the residual phase difference is lowered, and the film temperature is made high. When the rolling or the like is performed, peeling failure of the contact roll and the film is liable to occur, but the peeling failure can be effectively removed by the present invention. The above-mentioned constitution applies the release-adjusting agent to the contact roller 6, but the release-adjusting agent can also be applied to both surfaces of the contact roller 6 and the casting roller 5, and the adhesion of the film to the casting roller 5 is adjusted to be larger than The adhesive force of the film and the contact roll 6 can suppress the peeling failure of the contact roll 6 and the film at the time of peeling. The release agent of the present invention is a material which improves the release property of the contact roll 6 from the film, that is, It is not particularly limited and may be liquid or solid, and the product is preferably one which does not affect the necessary optical film properties. More preferably, the same material as that used for the optical film is used as a mold release adjuster. When a release property adjusting agent of the same material as the additive is used, even if the release property adjusting agent applied to the touch roll 6 is attached to the surface of the optical film, the optical film characteristics are hardly affected, and the contact can be effectively eliminated. The peeling of the roller 6 from the film is poor. Specific examples of the mold release modifier include polyoxyxane oil or dimethyloxane, I S] -11 - 201105480 methylene chloride, a plasticizer used as an additive for an optical film, an ultraviolet absorber, and the like. Further, a liquid in which organic or inorganic fine particles are dispersed may also be used. The release point of the release modifier is preferably from 150 to 250 °C. When the boiling point is this range, the surface temperature of the contact roller on the surface of the contact roller 6 is lower than 150. Therefore, the release property adjuster becomes liquid or solid, and functions as a release property adjuster. 'The mold release agent adjusted to the surface of the film after being released from the contact roll 6 is subjected to a high temperature step. The step is set to be more than the boiling point to cause volatilization, and the release property adjuster does not remain on the surface of the film, and the performance of the optical film can be maintained, which is preferable. The release modifier is particularly preferably an ultraviolet absorber. Since the ultraviolet ray absorbing agent has a high peeling property and the release property is exhibited by a thin layer, the smoothness of the surface of the film after the release of the contact roll 6 is improved, which is preferable. Further, since the constituent material of the optical film originally used for the optical film is added, it is preferable since it is incorporated in the optical film without affecting the characteristics of the optical film in the production step. The coating film thickness of the release property adjusting agent applied to the surface of the contact roll is preferably from 0.05 to 1,000 / zm. When the coating film thickness is set to this range, coating is too small to cause coating failure or too large, so that the release property adjusting agent stays between the contact roller and the cooling roller, resulting in lateral unevenness or unevenness of the film. It is less dangerous and therefore better. The contact angle S1 between the surface of the casting roll 5 and the contact angle S2 between the surface of the contact roll 6 after application of the release agent is preferably 0.5° < S2_S1 < 100°. S 2-S 1 is set to this range, and it is possible to reduce the coating failure (〇.5° or less) in which the release property is adjusted to -12-201105480, and the coating unevenness of the release property adjuster becomes the film thickness. It is better to have a risk of (1 〇〇 or more). The contact angle between the light surface and the water is measured by using a fully automatic contact angle meter r CA-W type roll type (manufactured by Kyowa Interface Science Co., Ltd.) at 23 ° C, 50 % RH. . In order to take into consideration the change in the measurement enthalpy of pure water evaporation and the stability of the measurement, the measurement is completed within 5 seconds to 30 seconds after the dropping of the pure water droplets. The measurement is performed by the 0/2 method of obtaining the contact angle from the angle of the solid surface to the line connecting the left and right end points of the droplet to the apex. The axial direction of the roller was measured at a right angle, and the amount of dripping was set to 70^1. The measurement was performed at the center of the measuring roller and at the position of 5 cm at the left and right end portions, and each of the circumferential directions of each of 90 degrees was 12 places. , using this average 値 as the contact angle. When the conveying tension of the film-like melt in the state where the contact roller 6 is pressed against the casting roll 5 is T1, and the conveying tension T2 of the film-like melt in a state where the contact roller 6 is not pressed against the casting roller 5, The enthalpy of T1-T2 is preferably from 1 to 2 50 N. The measurement of the conveyance tension is performed by loading a load gauge for taking the load in the vertical direction at both ends of the shaft of the nearest roller on the flow side below the casting roller 5, and calculating the respective loads when the contact roller 6 is pressed or not pressed against the casting roller 5. The difference between the counts and the total is ΤΙ-Τ'2. When the 値1 to Τ2 of the difference in the conveyance tension is set in the above range, the film (the film-like melt after curing to some extent) when peeled off by the contact roll 6 is not uneven (uniform), and there is no excessive stretching, so The film thickness may be uneven due to the deviation or the stretching may cause breakage, etc., and may be sent to the contact roller 6 in a stable manner.

F -13- 201105480 剝離的薄膜。特別是製造膜厚爲40 /z m以 時,可使由接觸輥6之剝離性良好,同時搬 範圔內時,可得到更安定之薄膜搬送,無橫 不均之平滑的薄膜,故較佳。 如上述,使用本發明之光學薄膜之製造 消除接觸輥與薄膜之剝離不良,在薄膜表面 薄膜幅方向之線條狀不均,在表面產生凹凸 均)或延遲不均的光學薄膜。 特別是將接觸輥表面加工成鏡面時,或 性金屬輥時,或提高由流延模擠出之熔融物 接觸輥與薄膜之黏著性升高,但是藉由本發 可改善接觸輥與薄膜之剝離不良,可得到薄 不均或延遲不均的光學薄膜。 以下詳細說明本發明之光學薄膜的製造 本發明之光學薄膜之製造方法中,熱可 之製膜方法係使用將溶融樹脂流延製膜之溶 來製膜。 本發明之光學薄膜之主材料較佳爲製造 膜之接著性佳,光學上透明等。 只要是具有上述性質的熱可塑性樹脂薄 別限定’例如有纖維素二乙酸酯薄膜、纖維 膜、纖維素乙酸酯丁酸酯薄膜、纖維素乙酸 等纖維素酯系薄膜、聚酯系薄膜、聚碳酸酯 酯系薄膜、聚颯(也包括聚醚楓)系薄膜、 下的光學薄膜 送張力在上述 向不均或延遲 方法,可得到 無橫向不均( ,可確認的不 接觸輥使用彈 的溫度時等, 明之製造方法 膜表面無橫向 方法。 塑性樹脂薄膜 融流延製膜法 容易,與偏光 膜時,即無特 素三乙酸酯薄 酯丙酸酯薄膜 系薄膜、聚芳 聚對苯二甲酸 -14- 201105480 乙二酯、聚萘二酸乙二酯等之聚酯薄膜、聚乙烯薄膜、聚 丙烯薄膜、賽璐玢、聚偏氯乙烯薄膜、聚乙烯醇薄膜'乙 烯乙烯醇薄膜、間規(syndio tactic )聚苯乙烯系薄膜、 聚碳酸酯薄膜 '環烯烴系聚合物薄膜、ZEONEX (商品名 、日本Zeon公司製)、ZEONOR (商品名、日本Zeon公 司製)、聚甲基戊烯薄膜.、聚醚酮薄膜、聚醚酮醯亞胺薄 膜、聚醯胺薄膜、氟樹脂薄膜、耐綸薄膜、聚甲基丙烯酸 甲酯薄膜、丙烯酸薄膜或玻璃板等。其中較佳爲纖維素酯 系薄膜、環烯烴聚合物薄膜、聚碳酸酯系薄膜、聚颯(包 括聚醚硼)系薄膜’本發明中,在製造上、成本面、透明 性、黏著性等觀點,特佳爲纖維素酯系薄膜、或含有環狀 燦烴系加成聚合物8〇%以上的樹脂薄膜。 構成本發明之光學薄膜的材料係含有此等樹脂、必要 時含有安定化劑、可塑劑 '紫外線吸收劑' 作爲滑劑之消 光劑、延遲控制劑。此等材料係依據目的之光學薄膜的要 求特性來適當選擇。 本發明之光學薄膜之材料使用纖維素樹脂時,其纖維 素樹脂係具有纖維素酯之構造,含有脂肪酸醯基、取代或 無取代之芳香族醯基中至少一種構造之纖維素單獨或混合 酸酯(以下僅稱爲「纖維素樹脂」),且爲非晶性者。「 非晶性」係指不規則的分子配置,不成爲結晶,而爲固體 的物質,表示原料時之結晶狀態者。 可用於本發明用之纖維素樹脂如日本特開2〇〇7-989 1 7號公報所例示,但是不限於此等者。 -15- 201105480 本發明所使用的纖維素酯作爲薄膜時的亮點異物較少 者爲佳。亮點異物係指將2片偏光板配置成正交(尼科耳 、Cross Nicols),於其間配置纖維素酯薄膜,偏光板保 護薄膜之遲相軸與其中一方之光源側之偏光板的透過軸平 行的位置時,在與另一方之偏光板的外側面垂直的位置觀 察時,造成漏光之原因的異物。此時評估用的偏光板較希 望爲無由亮點異物之保護薄膜所構成者,使用玻璃板保護 偏光子者較佳。纖維素樹脂所含之羥基的酯化部分未反應 爲亮點異物的原因之一,藉由使用亮點異物少的纖維素樹 脂及過濾經加熱熔融的纖維素樹脂除去異物,可降低亮點 異物。薄膜膜厚愈薄則每單位面積的亮點異物數愈少,薄 膜所含有之纖維素樹脂的含量愈少則有亮點異物愈少的傾 向。 輝點的個數係面積250mm2下,可以偏光尼科耳狀態 確認的大小爲5〜50 /z m的亮點爲300個以下,50 # m以 上之亮點較佳爲〇個。更佳爲5〜5〇em之亮點爲200個 以下。 亮點較多時,對液晶顯示器之圖像有極大的影響。相 位差薄膜作爲偏光板保護薄膜產生功能時,此亮點之存在 係造成雙折射之混亂的重要原因,對圖像有極大的不良影 響。 藉由熔融過濾去除亮點異物時,包括亮點異物之除去 步驟,可連續實施熔融流延的製膜步驟。 含有藉由熱熔融之亮點異物之濾過步驟的融融流延製 -16- 201105480 膜法係以後述的可塑劑與纖維素樹脂作爲組成 於未添加可塑劑的體系,使熱熔融溫度降低的 高亮點異物之除去效率及避免熱分解的觀點, 法。後述之其他的添加劑爲紫外線吸收劑及消 混合者也可同樣進行過濾。 濾材係較佳爲使用玻璃纖維、纖維素纖維 氟化乙烯樹脂等之氟樹脂等以往習知的濾材, 用陶瓷、金屬等。絕對過濾精確度係使用50 ,較佳爲30ym以下者,更佳爲l〇#m以下 5 // m以下者。此等可適當的組合後使用。 薄膜構成材料之纖維素樹脂以外的構成材 均一混合,在加熱時之熔融性方面可賦予均一 適當選擇纖維素樹脂以外之高分子材料或 維素樹脂混合。這種高分子材料或寡聚物較佳 樹脂相溶性優異者,做成薄膜時之全可 400nm〜800nm)的透過率爲 80%以上,較佳f ’更佳爲92 %以上。混合纖維素樹脂以外之 或寡聚物之至少1種以上之目的係包括爲了提 時之黏度控制或薄膜加工後之薄膜物性的意義 材料或寡聚物係也可含有其他添加劑的槪念。 其次,說明光學薄膜所用的添加劑。此等 用於脫模性調整劑。 適用的可塑劑較佳爲使用例如磷酸酯系有 酯、三甲酚磷酸酯、甲酚二苯基磷酸酯、辛基 物時,相較 觀點,從提 爲較佳的方 光劑經適當 、濾紙、四 但特佳爲使 # m以下者 者,更佳爲 料與該樹脂 的熔融性。 寡聚物與纖 爲與纖維素 見區域( I 90%以上 高分子材料 高加熱熔融 。此筒分子 之添加劑可 三苯基磷酸 二苯基磷酸 -17- 201105480 醋、二苯基聯苯基磷酸酯、三辛基磷酸酯、三丁基磷酸酯 等、酞酸酯系有二乙基酞酸酯、二甲氧基乙基酞酸酯、二 甲基酞酸酯、二辛基酞酸酯、二丁基酞酸酯、二-2-乙基 己基酞酸酯等、乙醇酸酯系有甘油三乙酸酯 '甘油三丁酸 酯、丁基酞醯基丁基乙醇酸酯、乙基酞醯基乙基乙醇酸酯 、甲基酞醯基乙基乙醇酸酯、丁基酞醯基丁基乙醇酸酯等 〇 上述之可塑劑必要可倂用2種類以上。此時,磷酸醋 系可塑劑之使用比率設定爲50質量%以下,結果不易產 生纖維素酯系樹脂薄膜之水解,耐久性優異,故較佳。磷 酸酯系可塑劑比率較少較佳,特別是僅使用酞酸酯系或乙 醇酸酯系可塑劑更佳。 爲了將吸水率及水分率設定在特定範圍內,因此較佳 之可塑劑之添加量係相對於纖維素酯系樹脂之質量%爲 3〜30質量%,更佳爲1〇~25質量%,更佳爲15〜25質量 %。其中可塑劑之添加量超過30質量%時,纖維素酯系 樹脂薄膜之機械強度·尺寸安定性會變差,故不佳》 氧化防止劑較佳爲受阻酚系化合物,具體例有2,6-二-第三丁基對甲酚、季戊四醇基四〔3-(3,5-二-第三丁 基-4-羥基苯基)丙酸酯〕、三乙二醇雙〔3-(3-第三丁 基-5-甲基-4-羥基苯基)丙酸酯〕、1,6-己二醇·雙〔3-( 3,5-二-第三丁基-4-羥基苯基)丙酸酯〕、2,4-雙-(正辛 基硫代)-6-(4-羥基-3,5-二-第三丁基苯胺基)-1,3,5-三 嗪、2,2-硫代-二伸乙基雙〔3- (3,5-二-第三丁基-4-羥基 -18 - 201105480 苯基)丙酸酯〕、十八烷基_3· ( 3,5-二-第三丁基-4-羥基 苯基)丙酸酯、1,3,5-三甲基-2,4,6-三(3,5-二-第三丁基-4_羥基苄基)苯及三(3,5·二-第三丁基-4-羥基苄基)異 氰尿酸酯等。特佳爲2,6-二-第三丁基-對甲酚、季戊四醇 基四〔3-(3,5_二-第三丁基-4-羥基苯基)丙酸酯〕及三 乙二醇雙〔3- (3-第三丁基-5-甲基-4-羥基苯基)丙酸酯 〕。又’可倂用例如N,N,-雙〔3- ( 3,5-二-第三丁基-4-羥 基苯基)丙醯基〕肼等之肼系之金屬惰性劑或三(2,4-二-第三丁基苯基)亞磷酸鹽(phosphite)等之磷系加工安定 劑。此等化合物之添加量爲了得到效果,相對於纖維素酯 系樹脂以質量比率表示較佳爲 lppm〜1 ·0 % ,特佳爲 10〜1OOOppm 〇 纖維素酯系樹脂中較佳爲添加紫外線吸收劑。紫外線 吸收劑從防止液晶劣化的觀點,較佳爲使用波長3 70nm 以下之紫外線吸收能優良,且從良好之液晶顯示性的觀點 ,波長400nm以上之可見光吸收較少者。 特佳爲波長3 70nm之紫外線的透過率爲10%以下者 ,更佳爲該透過率爲5%以下,更佳爲2%以下。 使用的紫外線吸收劑例如有氧基二苯甲酮系化合物、 苯並三唑系化合物、水楊酸酯系化合物、二苯甲酮系化合 物、氰基丙烯酸酯系化合物、鎳錯鹽系化合物等,但不限 於此等。 此等紫外線吸收劑使用1種以上較佳,可含有2種以 上不同的紫外線吸收劑。F -13- 201105480 Peeled film. In particular, when the film thickness is 40/zm, the peeling property by the contact roll 6 can be improved, and when the film is conveyed, a more stable film can be conveyed, and a smooth film having no unevenness is obtained. . As described above, the optical film of the present invention is used to eliminate the peeling failure of the contact roll and the film, the unevenness of the line on the surface of the film in the direction of the film, and the unevenness of the surface or unevenness of the optical film. In particular, when the surface of the contact roll is processed into a mirror surface, or when a metal roll is used, or the adhesion of the melt contact roll extruded from the casting die is increased, the peeling of the contact roll and the film can be improved by the present invention. Poor, an optical film with uneven thickness or uneven retardation can be obtained. Hereinafter, the production of the optical film of the present invention will be described in detail. In the method for producing an optical film of the present invention, the film forming method of heat can be formed by dissolving a film formed by casting a molten resin. The main material of the optical film of the present invention is preferably excellent in adhesion to a film, optically transparent, and the like. As long as it is a thermoplastic resin having the above properties, it is defined as, for example, a cellulose diacetate film, a fiber film, a cellulose acetate butyrate film, a cellulose acetate film such as cellulose acetate, or a polyester film. The polycarbonate film-based film, the polyfluorene-based film (including the polyether maple)-based film, and the lower optical film are fed in the above-mentioned unevenness or retardation method, and no lateral unevenness can be obtained (the use of the non-contact roller can be confirmed) When the temperature of the bomb is used, etc., there is no lateral method on the surface of the film. The plastic resin film is easy to melt and cast, and when it is polarized, there is no thin film of triacetate film. Polyterephthalic acid-14- 201105480 Polyester film of ethylene glycol, polyethylene naphthalate, polyethylene film, polypropylene film, cellophane, polyvinylidene chloride film, polyvinyl alcohol film 'ethylene Vinyl alcohol film, syndiotactic polystyrene film, polycarbonate film 'cycloolefin polymer film, ZEONEX (trade name, manufactured by Zeon Corporation, Japan), ZEONOR (trade name, Japan Zeon Corporation) System), polymethylpentene film, polyetherketone film, polyether ketoximine film, polyamide film, fluororesin film, nylon film, polymethyl methacrylate film, acrylic film or glass A plate or the like is preferably a cellulose ester film, a cycloolefin polymer film, a polycarbonate film, or a polyether (including a polyether boron) film. In the present invention, in terms of production, cost, transparency, Particularly, a cellulose ester-based film or a resin film containing a cyclic hydrocarbon-based addition polymer of 8% or more is particularly preferable. The material constituting the optical film of the present invention contains these resins and, if necessary, contains a resin film. The stabilizer and the plasticizer 'ultraviolet absorber' are used as a matting agent and a retardation controlling agent for the slipping agent. These materials are appropriately selected depending on the desired characteristics of the optical film of the object. When the material of the optical film of the present invention is a cellulose resin a cellulose resin having a structure of a cellulose ester, comprising a cellulose alone or a mixed acid ester of at least one of a fatty acid sulfhydryl group, a substituted or unsubstituted aromatic fluorenyl group (hereinafter only It is called "cellulose resin" and is amorphous. "Amorphous" refers to an irregular molecular arrangement, and is not a crystal, but a solid substance, which indicates the crystal state of the raw material. The cellulose resin for use in the invention is exemplified as disclosed in Japanese Laid-Open Patent Publication No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. The bright spot foreign matter means that two polarizing plates are arranged in a cross direction (Nico, Cross Nicols), and a cellulose ester film is disposed therebetween, and the retardation axis of the polarizing plate protective film and the light source side of one of the light sources are polarized. When the position of the plate passing through the axis is parallel, when it is observed at a position perpendicular to the outer side surface of the other polarizing plate, foreign matter causing light leakage is caused. In this case, the polarizing plate for evaluation is preferably formed of a protective film which is free from foreign matter, and it is preferable to use a glass plate to protect the polarizer. One of the causes of the esterification of the hydroxyl group contained in the cellulose resin is that it is a bright spot foreign matter, and the foreign matter can be reduced by using a cellulose resin having a small amount of foreign matter and a cellulose resin which is heated and melted to remove foreign matter. The thinner the film thickness, the less the number of bright foreign matter per unit area, and the less the content of the cellulose resin contained in the film, the less the tendency of bright foreign matter. The number of bright spots is 250 mm2, and the bright spot with a size of 5 to 50 /z m which can be confirmed by the polarized Nicols state is 300 or less, and the bright spot of 50 # m or more is preferably one. More preferably, the highlight of 5~5〇em is 200 or less. When there are many bright spots, it has a great influence on the image of the liquid crystal display. When the phase difference film functions as a polarizing plate protective film, the presence of this bright spot is an important cause of the disorder of birefringence, which has a great adverse effect on the image. When the bright foreign matter is removed by melt filtration, the step of removing the foreign matter including the bright spot is carried out, and the film forming step of the melt casting can be continuously performed. Melt-casting process containing a filtration step by hot-melting bright-spotted foreign matter -16-201105480 Membrane method, a plasticizer and a cellulose resin, which will be described later, are used as a composition in a system in which no plasticizer is added, and the hot melting temperature is lowered. The removal efficiency of foreign matter and the viewpoint of avoiding thermal decomposition. The other additives described later may be filtered in the same manner as the ultraviolet absorber and the demixer. The filter medium is preferably a conventional filter material such as a fluororesin such as glass fiber or cellulose fiber fluorinated vinyl resin, and ceramic or metal. The absolute filtration accuracy is 50, preferably 30 μm or less, and more preferably l〇#m or less 5 // m or less. These can be used in appropriate combinations. The constituent materials other than the cellulose resin of the film constituting material are uniformly mixed, and the polymer material other than the cellulose resin or the vegetal resin can be appropriately selected in terms of the meltability at the time of heating. Such a polymer material or oligomer preferably has a resin compatibility of at least 400 nm to 800 nm when formed into a film, and preferably has a transmittance of 80% or more, more preferably 92% or more. At least one of the other than the cellulose resin or the oligomer is included for the purpose of improving the viscosity of the film or the film properties after the film processing. The material or the oligomer system may also contain other additives. Next, the additives used for the optical film will be explained. These are used for mold release modifiers. Suitable plasticizers are preferably used, for example, a phosphate ester-based ester, a tricresol phosphate, a cresol diphenyl phosphate, or an octyl group. It is better to make the melting of the resin better than the one below #m. The oligomer and the fiber are in the area of the cellulose (I 90% or more of the polymer material is heated and melted. The additive of the tube molecule can be triphenylphosphoric acid diphenyl phosphate-17-201105480 vinegar, diphenylbiphenyl phosphate Ester, trioctyl phosphate, tributyl phosphate, etc., phthalate esters are diethyl phthalate, dimethoxyethyl phthalate, dimethyl phthalate, dioctyl phthalate , dibutyl phthalate, di-2-ethylhexyl decanoate, etc., glycolic acid esters are triacetin 'glycerol tributyrate, butyl decyl butyl glycolate, ethyl酞醯 乙基 ethyl glycolate, methyl decyl ethyl glycolate, butyl decyl butyl glycolate, etc. The above plasticizers may be used in more than two types. At this time, the phosphate vinegar system When the use ratio of the plasticizer is 50% by mass or less, hydrolysis of the cellulose ester-based resin film is less likely to occur, and durability is excellent, and the ratio of the phosphate-based plasticizer is less preferable, and in particular, only the phthalate is used. A glycolic acid-based plasticizer is preferred. In order to set the water absorption rate and moisture content to a specific range Therefore, the amount of the plasticizer to be added is preferably from 3 to 30% by mass, more preferably from 1 to 25% by mass, even more preferably from 15 to 25% by mass, based on the mass% of the cellulose ester-based resin. When the amount is more than 30% by mass, the mechanical strength and dimensional stability of the cellulose ester resin film are deteriorated. Therefore, the oxidation inhibitor is preferably a hindered phenol compound, and specific examples are 2,6-di- Tributyl-p-cresol, pentaerythritol tetrakis[3-(3,5-di-t-butyl-4-hydroxyphenyl)propionate], triethylene glycol bis[3-(3-third butyl) 5-methyl-4-hydroxyphenyl)propionate], 1,6-hexanediol·bis[3-(3,5-di-t-butyl-4-hydroxyphenyl)propionic acid Ester], 2,4-bis-(n-octylthio)-6-(4-hydroxy-3,5-di-t-butylanilino)-1,3,5-triazine, 2,2 - thio-di-extension ethyl bis[3-(3,5-di-t-butyl-4-hydroxy-18 - 201105480 phenyl)propionate], octadecyl_3· (3,5 -di-t-butyl-4-hydroxyphenyl)propionate, 1,3,5-trimethyl-2,4,6-tris(3,5-di-t-butyl-4-hydroxyl Benzyl)benzene and tris(3,5·di-t-butyl-4-hydroxyl Benzyl)isocyanurate, etc. Particularly preferred is 2,6-di-t-butyl-p-cresol, pentaerythritol tetra[3-(3,5-di-t-butyl-4-hydroxybenzene) Propionate] and triethylene glycol bis[3-(3-tert-butyl-5-methyl-4-hydroxyphenyl)propionate]. Also, for example, N, N, - A metal inert agent or tris(2,4-di-t-butylphenyl) of bis[3-(3,5-di-t-butyl-4-hydroxyphenyl)propanyl]anthracene A phosphorus-based processing stabilizer such as phosphite. In order to obtain an effect, the amount of such a compound is preferably from 1 ppm to 1% by weight, particularly preferably from 10 to 1,000 ppm, based on the mass ratio of the cellulose ester resin. Preferably, the cellulose ester resin is added with ultraviolet light absorption. Agent. From the viewpoint of preventing deterioration of the liquid crystal, the ultraviolet absorber is preferably excellent in ultraviolet absorption energy at a wavelength of 3 to 70 nm or less, and has a small absorption of visible light having a wavelength of 400 nm or more from the viewpoint of good liquid crystal display properties. Particularly preferably, the transmittance of ultraviolet rays having a wavelength of 3 to 70 nm is 10% or less, and more preferably the transmittance is 5% or less, more preferably 2% or less. The ultraviolet absorber to be used is, for example, an oxybenzophenone-based compound, a benzotriazole-based compound, a salicylate-based compound, a benzophenone-based compound, a cyanoacrylate-based compound, a nickel-salted salt-based compound, or the like. , but not limited to this. These ultraviolet absorbers are preferably used singly or in combination of two or more kinds, and may contain two or more kinds of ultraviolet absorbers.

-19- 201105480 較適用的紫外線吸收劑係苯並三唑系紫外線吸收劑或 一本甲酮系紫外線吸收劑等。於纖維素酯系樹脂薄膜中添 加不必要之著色更少的苯並三唑系紫外線吸收劑的態樣特 佳。 紫外線吸收劑之添加方法係將紫外線吸收劑溶解於醇 或一氯甲烷、二氧雜戊烷等之有機溶劑後,添加於膠漿中 或直接添加於膠漿組成中。如無機粉體不溶解於有機溶劑 者’可使用分散機或混砂機分散於有機溶劑與纖維素酯系 樹脂中,然後添加於膠漿中。 紫外線吸收劑之使用量係相對於纖維素酯系樹脂之質 量%爲0.1〜2_5質量% ’較佳爲〇_5〜2.0質量%,更佳爲 0.8~2_0質量%。紫外線吸收劑之使用量超過2 5質量% 時’纖維素醋系樹脂薄膜之透明性有變差的傾向,故不佳 〇 纖維素酯系樹脂薄膜爲了防止薄膜彼此之黏貼或賦予 滑性’容易使用操作時,可添加微粒子作爲消光劑。 微粒子之種類可爲無機化合物或有機化合物。無機化 合物之微粒子例如有二氧化矽、二氧化鈦、氧化鋁、氧化 锆、氧化錫等微粒子。其中較佳爲含有矽原子的化合物, 特佳爲二氧化矽。二氧化矽微粒子例如有AERO SIL股份 公司製之 AEROSIL-200、200V、300、R972 ' R972V、 R974、R976、R976S、R202 ' R812、R805、0X50、 TT600、RY50、RX50、NY50、N A X 5 0、N A 5 0 Η、N A 5 0 Y 、NX90、 RY200S、RY200、RX200、R8200、 RA200H、 -20- 201105480 RA200HS > NA200Y 、 R816 、 R104 、 RY300 、 RX300 ' R l 06等。此等中,從控制分散性或粒徑的觀點,較佳爲 AEROSIL-200V、R972V。 薄膜中之微粒子的平均粒徑從賦予滑性及確保透明性 的觀點,較佳爲50nm〜2;/m。較佳爲1 0 0nm~ 1 OOOnm,更 佳爲 100nm~500nm。薄膜中之平均粒徑係拍攝剖面照片 進行觀察面來確認。 微粒子的情形,1次粒徑、分散於溶劑後的粒徑、添 加於薄膜後的粒徑經常變化,重要的是控制最終在薄膜中 ’微粒子與纖維素酯系樹脂複合凝集所形成的粒徑。 微粒子的添加量係相對於纖維素酯系樹脂薄膜爲 〇·02〜0.5質量%,較佳爲0.04〜0.3質量%。 此等添加於光學薄膜的添加劑塗佈於接觸輥表面,使 接觸輥與薄膜之黏著性小於冷卻輥與薄膜之黏著性,可改 善接觸輥與薄膜之脫模性。 圖2係使用溶融流延製膜法實施本發明之光學薄膜之 製造方法之裝置之第一實施形態的槪略流程圖。 揭露薄膜(熔融物)最初接觸鑄造輥5表面的點(Ρ 1 )與薄膜接觸於接觸輥(挾壓旋轉體)6表面的點(Ρ2) 不同的實施形態,但是有時薄膜最初接觸鑄造輥5表面的 點(Ρ1)與薄膜接觸於接觸輥(挾壓旋轉體)6表面的點 (Ρ2 )相同。此外,有時薄膜先與接觸輥6接觸後,再與 Ρ2接觸。 本實施形態係混合含有纖維素樹脂等樹脂之薄膜材料 -21 - 201105480 得到樹脂混合物後,使用擠出機1由流延模4熔融擠出至 鑄造輥5上。接觸輥6表面係藉由脫模性調整劑塗佈裝置 1 〇〇塗佈所定量之紫外線吸收劑作爲脫模性調整劑1 04。 擠出後之薄膜狀之熔融物外接鑄造輥5,同時藉由接觸輥 6對鑄造輥5表面以所定壓力按壓。依序外接於冷卻輥7 、8的輥,進行冷卻固化,以剝離輥9剝離。剝離後之薄 膜17係藉由縱延伸裝置10與橫延伸裝置20,在薄膜之 縱(搬送方向)及橫(寬度方向)進行延伸後,以捲繞裝 置6 0捲繞。 以下詳細說明。 被流延模4擠出之薄膜狀之含有熱可塑性樹脂的熔融 物係被擠出至具有冷卻功能之鑄造輥5上,被接觸輥6挾 壓,同時冷卻、面矯正。鑄造輥5及接觸輥6不限於輥, 可爲轉筒或帶等。 鑄造輥5之溫度較佳係設定爲樹脂混合物之玻璃轉化 溫度(Tg )以下、添加劑之熔點以上^ 接觸輥6係對於薄膜,由鑄造輥5之相反側於鑄造輥 5之方向挾壓薄膜爲目的之旋轉體。 接觸輥6之表面較佳爲金屬,厚度爲lmm~10mm。較 佳爲2mm〜6mm。挾壓旋轉體之表面施力[]鍍絡等處理,表 面粗度係最大高度Ry較佳爲〇·1;ζπι以下,更佳爲0.05 /zm以下。輥表面越平滑時,所得之薄膜表面也越平滑 挾壓步驟中,接觸輥6較佳爲外周具有金屬圓筒之彈 性輥(彈性金屬輥)所構成者。 -22- 201105480 換言之,接觸輕6之壓力不均~時,薄膜產生配向不 均,此乃是正交(Cross Nicols)下,成爲明暗不均。欲 以均一的壓力對薄膜進行面矯正時,較佳爲如上述之外周 具有金屬圓筒之彈性的接觸輥。 接觸輥6之表面的金屬材質係要求平滑,且具有適度 彈性及耐久性。較佳爲使用以碳鋼、不鏽鋼、鈦、電鑄法 製造之鎳等。欲提高其表面之硬度' 或改良與樹脂之脫模 性’因此施以鍍硬鉻、或鍍鎳、鍍非晶質鉻等、陶瓷火焰 噴射等表面處理爲佳。經表面加工後的表面進一步地硏磨 ’成爲上述表面粗度爲佳。 接觸輥6係金屬製外筒與內筒之雙重構造,使冷卻流 體流通於其間,具有空間的二重筒的構成。 內筒爲碳鋼、不鏽鋼、鋁、鈦等輕質,具有剛性之金 屬製內筒較佳。使內筒具有剛性,可抑制輥之旋轉晃動。 內筒之筒厚爲外筒之2〜1 0倍時,可得到充分的剛性。內 筒可進一步被聚矽氧烷、氟橡膠等樹脂製彈性材料所覆蓋 〇 使冷卻流體流動的空間構造係只要是可均勻控制輥表 面溫度者即可,例如向寬度方向往返可互相流動,形成螺 旋狀流動,即可控制輥表面之溫度分佈之微小溫度。冷卻 流體並無特別限制,配合使用之溫度範圍可使用水或油。 接觸輥6係設定成中央部之外徑大於兩端部之外徑的 太鼓型。接觸輥一般係將其兩端部以加壓手段按壓薄膜, 此時因接觸輥可撓性,因此有越靠端部,越強力按壓的現 -23- 201105480 象。輥設定成太鼓型,可得到高度均一的按壓。 接觸輥6之直徑較佳爲200mm~500mm的範圍。接觸 輥6之有效寬度必須大於挾壓之薄膜寬。藉由接觸輥6之 中央部之半徑與端部之半徑之差(以下稱爲最高量)可防 止在薄膜中央部所發生之線條等之不均。最高量較佳爲 50〜3 00 v m的範圍。 鑄造輥5與接觸輥6係設置於相對於薄膜之平面爲相 反側的位置,以挾壓薄膜。鑄造輥5與接觸輥6即使與薄 膜以面接觸或以線接觸均可。 接觸輥6之表面在挾壓鑄造輥5上之薄膜之前,藉由 脫模性調整劑塗佈裝置1 00塗佈所定量之脫模性調整劑 1 〇4。脫模性調整劑〇4之塗佈已於先前詳細說明,在此省 略說明。 本實施形態之光學薄膜之製造方法中,熔融擠出之條 件可與其他聚酯等之熱可塑性樹脂所使用的條件相同的狀 態下進行。材料較佳爲預先乾燥。真空或減壓乾燥機或除 濕熱風乾燥機等使水分乾燥至lOOOppm以下,較佳爲 200ppm 以下。 例如使用擠出機1在擠出溫度200〜3 0CTC下,將以熱 風或真空或減壓下乾燥的纖維素酯系樹脂進行熔融,以葉 片型過濾器2等過濾除去異物。 由供料斗(圖示省略)導入擠出機1時,較佳爲於真 i下或減壓下或惰性氣體氣氛下,防止氧化分解等。 未預先混合可塑劑等的添加劑時,可於擠出機之途中 24- 201105480 混煉。欲使其能均勻添加,較佳爲使用靜態混合機3等的 混合裝置。 纖維素樹脂等之樹脂與其他必要而添加的安定化劑, 較佳爲熔融前混合。可藉由混合機等進行混合,或如前述 ,在纖維素樹脂等之樹脂調製過程中混合。使用混合機時 ’可使用V型混合機、圓錐螺旋型混合機、水平圓筒型 混合機等一般的混合機。 如上述混合薄膜構成材料後,將該混合物使用擠出機 1直接熔融後製膜,但是也可一旦將薄膜構成材料顆粒化 後’將該顆粒以擠出機1熔融製膜。此外,薄膜構成材料 含有熔點不同之複數材料時,也可以僅熔點較低之材料熔 融的溫度’ 一旦製作所謂的米粥狀的半熔融物,將半熔融 物投入於擠出機1後製膜。薄膜構成材料中含有容易熱分 解的材料時,爲了減少溶融次數,較佳爲不製作顆粒,直 接製膜的方法、或製作如上述米粥狀之半熔融物後製膜的 方法。 擠出機1可使用可由市面上取得之各種擠出機,但以 熔融混煉擠出機爲佳,可爲單軸擠出機或雙軸擠出機。不 由薄膜構成材料製作顆粒,而直接製膜時,因需要適當的 混煉度,因此使用雙軸擠出機爲佳,即使單軸擠出機可將 螺旋形狀變更爲Maddock型、Unimelt型、Dulmage等混 煉型之螺旋,可得到適度混煉,故可使用。薄膜構成材料 一旦使用顆粒或米粥狀之半熔融物時,可使用單軸擠出機 或雙軸擠出機。 -25- 201105480 擠出機1內及擠出後之冷卻步驟可以氮氣體等之惰性 氣體取代、或藉由減壓降低氧濃度爲佳。 擠出機1內之薄膜構成材料的熔融溫度係依薄膜構成 材料的黏度或吐出量、製造之薄片厚度等,因而較佳條件 也不同’一般對於薄膜(樹脂混合物)之玻璃轉化溫度 Tg而言爲Tg以上、Tg+io〇°c以下,較佳爲Tg+urc以上 、Tg + 90°C以下。擠出時之熔融黏度爲1〜lOOOOPa. s,較 佳爲10〜10 OOPa’s。又,擠出機1內之薄膜構成材料之滯 留時間較短者爲佳,一般爲5分鐘以內,較佳爲3分鐘以 內,更佳爲2分鐘以內。滯留時間係受擠出機1之種類、 擠出條件左右,但是可藉由調整材料之供給量或L/D、螺 轉數、螺旋之溝深度等縮短滯留時間。 擠出機1之螺旋形狀或轉數等藉由薄膜構成材料的黏 度或吐出量等來適當選擇。本實施形態中,擠出機1之剪 切速度爲1/秒- 1 0000/秒,較佳爲5/秒〜1 000/秒,更佳爲 10/秒〜100/秒。擠出機1可使用一般塑膠成形機之市售的 擠出機。 由擠出機1所擠出的薄膜構成材料係被送至流延模4 ,由流延模4擠出成薄膜狀。 由擠出機1所吐出之熔融物供給流延模4。流延模4 只要是用於製造薄片或薄膜者,即無特別限定。流延模4 之材質例如有將硬鉻、碳化鉻、氮化鉻、碳化鈦、碳氮化 鈦、氮化鈦、超鋼、陶瓷(碳化鎢、氧化鋁、氧化鉻)等 進行溶射或鍍敷’然後施加表面加工爲拋光’使用# 1000 -26- 201105480 號以下之磨石的硏1磨,使用000號以上之鑽石磨石之平 面切割(切割方向係與樹脂的流向呈垂直的方向)、電解 硏磨、電解複合硏磨等加工者等° 流延模4之糢唇(1 ip )部之較佳材質係與流延模4 相同。又,模唇音卩表面精度較佳爲〇 · 5 s以下’更佳爲 0.2S以下。 本實施形態具有將熔融之樹脂混合物由裝設於擠出機 之流延模4擠出成薄膜狀樹脂,然後使被擠出之薄膜狀樹 脂與鑄造輥5及接觸輥6密著,加壓後取得的步驟。 薄膜狀之熔融物最初與鑄造輥5表面接觸後至接觸接 觸輥6表面爲止之溫度下降,較佳爲20°C以內。薄膜最初 與鑄造輥5表面接觸後至接觸接觸輥6表面爲止之溫度下 降太大時,因不均-的收縮造成膜厚不均變大。此外,薄 膜接觸接觸輥6之時點的溫度太低時,因薄膜之黏度高, 即使以接觸輥6狹壓仍對於薄膜之平面性或膜厚不均之矯 正仍不充分。 鑄造輥5、接觸輥6之較佳的材質例如有碳鋼、不繡 鋼等。表面精度越高越佳,表面粗度在最大高度Ry較佳 爲0 · 1 // m以下,更佳爲〇.〇5/zm以下。 接觸輥6係藉由按壓手段將薄膜緊壓於鑄造輥5較佳 。此時之接觸輥6緊壓薄膜之線壓可藉由油壓活塞等來調 整’較佳爲0.1~100N/mm ’更佳爲1〜50N/mm。 鑄造輥5或接觸輥6爲了提高與薄膜之接著均—性, 可將輥之兩端直徑變細或具有撓性的輥面。 -27- 201105480 由流延模4之開口部(唇部)至鑄造輥5之部分減壓 至7 OkP a以下時,發現上述之模線的矯正效果更大。較佳 爲減壓係50kPa以上7〇kPa以下。由流延模4之唇部至鑄 造輥5之部分的壓力保持在7 OkPa以下的方法無特別限定 ,例如有由流延模4至輥周邊以耐壓構件覆蓋,進行減壓 等的方法。此時,吸引裝置係爲了避免裝置本身成爲昇華 物之附著場所,而實施以加熱器加熱等的措施較佳。吸引 壓太小時,無法有交^的吸引昇華物,因此必須有適當的吸 引壓。 由流延模4將溶融狀態之薄膜狀之纖維素酯系樹脂依 序密著於鑄造輥5、冷卻輥7、及冷卻輥8進行搬送同時 冷卻固化,得到纖維素酯系樹脂薄膜1 7。 圖2所示之本發明的實施形態中,由冷卻輥8藉由剝 離輥9剝離後之冷卻固化的薄膜17被導入於縱延伸裝置 1〇中,在搬送方向(MD方向)被輥延伸。 接著’縱延伸後之薄膜導入於橫延伸裝置(拉幅器) 20’將薄膜17在橫方向(寬度方向)延伸。藉由此橫延 伸使薄膜中之分子被配向。 橫延伸後’薄膜1 7之端部藉由切割機1 9切割成製品 之寬度剪裁後,藉由浮雕環(emboss ring) 53及背輥52 所構成之凸邊加工裝置,對薄膜兩端部施行浮雕加工( embossing加工),然後,藉由捲繞裝置6 0捲繞,防止光 學薄膜(原捲)F中I之黏貼或擦傷^ 浮雕加工的方法可藉由對於側面上具有凸凹圖型之金 -28- 201105480 屬環加熱或加壓來加工。薄膜兩端部之夾具的把持部分通 常會變形,無法作爲薄膜製品使用,故經切除後作爲原料 再利用。 使用之捲繞機可爲一般使用者,可以定張力(tension )法、定轉距法、錐度張力法、內部應力固定之程式張力 控制(program tension control)法等捲繞方法捲繞。 橫延伸後實施凸邊加工的步驟及切除薄膜端部之厚膜 部之切割加工步驟可在捲繞步驟前進行。 如上述,以本實施形態製造的光學薄膜作爲相位差薄 膜使用,以此相位差薄膜作爲偏光板保護薄膜時,該保護 薄膜之厚度較佳爲10〜500 // m。特別是下限爲20 # m以 上,較佳爲35 m以上。上限係150 m以下,較佳爲 120 m以下。特佳的範圍係35〜90 // m。相位差薄膜較厚 時,偏光板加工後之偏光板變太厚,用於筆記型電腦或攜 帶型電子機器的液晶顯示時,特別是不適用於薄型質輕的 目的。此外,相位差薄膜較薄時,很難展現相位差薄膜之 延遲,而且薄膜之透濕性升高,保護偏光子避免濕度的功 能降低,故不理想。 本發明對象之光學薄膜係液晶顯示器、電漿顯示器、 有機EL顯示器等之各種顯示器、特別是液晶顯示器用的 功能薄膜,包括偏光板保護薄膜、相位差薄膜、反射防止 薄膜、亮度提昇薄膜、視角擴大等的光學補償薄膜等、特 別是相位差薄膜。 E S:} -29- 201105480 (液晶顯示裝置) 含有以本發明之光學薄膜所構成之相位差薄膜的偏光 板,與一般的偏光板比,具有高的顯示品質,特別是適合 使用於多區域型的液晶顯示裝置,更佳爲適合使用於藉由 雙折射型之多區域型的液晶顯示裝置。 多區域化也適用於提高圖像顯示之對稱性,有各種的 方式「置田、山內:液晶,6 ( 3 ) ,303 ( 2002 )」。該液 晶顯示晶胞也記載於「山田、山原:液晶,7 ( 2 ) ,1 8 4 (2003 )」,但是不限於此等。 使用本發明之光學薄膜的偏光板係可有效的用於垂直 配向型所代表之 MVA(Multi-domein Vertical Alignment )型、特別是4分割之MVA型、藉由電極配置之多區域 化之公知的 PVA( Patterned Vertical Alignment)型、融 合電極配置與掌性(chiral)有巨的 CPA ( Continuous Pinwheel Alignment)型。此外,適用於 OCB (Optical Compensated Bend)型時,提案光學上具有雙軸性的薄膜 「T. Miyashita,T. Uchida:J. SID,3 ( 1 ) ,29 ( 1 995 ) 」,藉由使用本發明之光學薄膜的偏光板可具有顯示品質 效果。 只要藉由使用本發明之光學薄膜的偏光板可展現顯示 品質效果時,液晶型、偏光板之配置不受限定。 顯示晶胞之顯示品質係在人的觀察時,左右對稱較佳 。因此,顯示晶胞爲液晶顯示晶胞時,實質上,觀察側之 對稱性優先,可將區域形成多區域化。區域之分割可採用 -30- 201105480 公知方法,藉由2分割法、更佳爲4分割法考慮公知的液 晶型的性質來決定。 液晶顯示裝置也可作爲彩色化及動畫顯示用的裝置應 用’藉由本發明之光學薄膜改良顯示品質,藉由對比的改 善或提高偏光板的耐久性,可使眼睛不易疲勞且忠實的動 態圖像顯示。 液晶顯示裝置係將含有以本發明之光學薄膜所構成之 相位差薄膜的偏光板相對於液晶胞配置一片,或於液晶胞 兩側配置二片。此時偏光板所含之相位差薄膜側面向液晶 顯示裝置之液晶胞的方式使用,有助於提昇顯示品質。 偏光板中,從偏光子來看,在與相位差薄膜相反側的 面’使用纖維素衍生物的偏光板保護用薄膜,可使用泛用 的TAC薄膜等。位於遠離液晶胞側之偏光板保護薄膜係 在提高顯示裝置的品質上,可配置其他的功能性層。 本發明之光學薄膜,例如可賦予防反射、防眩、耐刮 傷、防污物附著、亮度提升的功能。可貼於偏光板表面, 但不限於此等。 製造相位差薄膜時,在延伸前及/或延伸後可塗設防 靜電層、硬塗層、易滑性層、黏著層、防眩層、阻隔層等 之功能性層。此時,必要時可實施電暈放電處理、電漿處 理、藥液處理等各種表面處理。 本發明之光學薄膜作爲相位差薄膜,用於偏光板的保 護薄膜時,偏光板的製作方法並沒有特別的限制,可以一 般的方法製作。例如有將所得之相位差薄膜進行鹼處理, -31 - 201105480 將聚乙烯醇薄膜浸漬於碘溶液中延伸製作之偏光子的兩面 使用完全皂化聚乙烯醇水溶液,於偏光子之兩面貼合偏光 板保護薄膜的方法,至少單面上’本發明之偏光板保護薄 膜之相位差薄膜直接貼合於偏光子。 實施如日本特開平-6-94915號公報、特開平6-118232號公號所記載之易黏著加工取代上述鹼處理,進 行偏光板加工。 偏光板係以偏光子及保護其兩面之保護薄膜所構成, 該偏光板之一面貼合保護薄膜,另一面貼合分隔薄膜所構 成。保護薄膜及分隔薄膜係用於偏光板出貨時,製品檢查 時等保護偏光板。此時,保護薄膜係爲了保護偏光板表面 而貼合的,保護薄膜係用於將偏光板貼合於液晶板之面的 相反面側。分隔薄膜係用於保護貼合於液晶板之黏著層, 可用於將偏光板貼合於液晶胞的面側。 【實施方式】 [實施例] 以下表示光學薄膜之製造方法之實施例、比較例。 (實施例1〜8 ) (樹脂混合物) 纖維素乙酸酯丙酸酯 89質量% (乙醯基取代度:1·4、丙醯基取代度:1.35、 數平均分子量:6 0 0 0 0 ) -32- 201105480 三羥甲基丙烷三苯甲酸酯 9質量% (可塑劑、熔點8 51:) (氧化防止劑)(IRGANOX XP 420/FD) 0.25 質量 % (Ciba Japan 公司製) 紫外線吸收劑 1.6質量% (TINUVIN 928、Ciba Japan 公司製、溶點 115 °C) 消光劑(氧化矽微粒子) 0.15質量% (seahoster KEP-30:日本觸媒股份公司製、平均粒徑 0.3 μηι ) 纖維素乙酸酯丙酸酯之乙醯基、丙醯基等之醯基取代 度測定係依據ASTM-D8 17-96所規定的方法測定。 將上述材料以V型混合機混合3 0分鐘後,使用裝設 有絞線(strand )模之雙軸擠出機,在氮氣氛下以23CTC 熔融製作長度4mm '直徑3mm之圓筒形的顆粒。所得之 顆粒的玻璃轉化點(Tg )爲1 3 5 °C。 (光學薄膜之製造) 將上述顆粒以100°C乾燥5小時,使含水率爲i〇〇ppm ,將該顆粒供給如圖2所示裝設有T模4之單軸擠出機! 進行製膜。熔融物中,樹脂以外之添加劑含有1 1質量% 〇 單軸擠出機1係螺旋徑90mm、L/D = 30、使擠出量成 爲140kg/h的方式調整螺旋的轉數。由材料供給口附近封 -33- 201105480 入氮氣體,使擠出機1內保持氮氣氛。擠出機1及T模4 係將溫度設定爲240°C "Τ模4係衣架型,寬爲1 500mm、 內壁上鍍硬鉻,加工成面粗度爲0. IS的鏡面。T模4之 模唇間隙設定爲2 m m。 如圖2所示,使T模4擠出之薄膜狀熔融物掉落於表 面溫度調整爲120°C之輥寬1 600mm之鍍鉻鏡面的鑄造輥 5上,同時藉由溫度調整爲120 °C之輥寬1600mm之接觸 輥(挾壓旋轉體)6按壓薄膜。 在接觸輥之表面,與鑄造輥5上之熔融物Y接觸之 P2位置更上流側,如圖1所示,藉由脫模性調整劑塗佈 裝置1 〇〇預先塗佈脫模性調整劑。脫模性調整劑塗佈裝置 1 〇〇係加溫成與接觸輥6相同溫度1 20°C。脫模性調整劑 係使用紫外線吸收劑TIN U V IN 9 2 8 ( T - 9 2 8 )與二甲基砂 氧烷、四氟化乙烯共聚合物。T-928與二甲基矽氧烷係以 液狀塗佈,四氟化乙烯共聚合物係相對於溶劑二甲苯1〇〇 質量份溶解20質量份進行塗佈。四氟化乙烯共聚合物係 分散於液體的狀態塗佈於接觸輥表面。塗佈於接觸_ 6之 塗佈厚度如表1 ’作爲實施例1〜8的製造條件。鑄造輥5 之表面與水之接觸角爲75° ’塗佈脫模性調整劑後之接觸 輥6之表面與水之接觸角係T-928爲95。、四氟化乙烯共 聚合物爲109°、二甲基矽氧烷爲120。^ 接觸輥(挾壓旋轉體)6係以5N/mm之線壓按壓薄 膜。 鑄造輥5係使用不鏽鋼,表面粗度係最大高度爲 -34- 201105480 0.1 v m以下》 接觸輥6係使用具備金屬外筒、內筒、空隙部之二重 筒構造者。金屬外筒之材質係不鏽鋼、表面粗度係最大高 度Ry爲0.〇5/zm以下,筒厚係3mm。內筒係鋁,筒厚爲 3 0mm。金屬外筒與內筒之空隙部爲5mm。此空隙部47內 有油流通,使金屬外筒之表面溫度爲120 °C» 被按壓於鑄造輥5與接觸輥(挾壓旋轉體)6的薄膜 ,接著依序外接於冷卻輥7、及冷卻輥8之輥,經冷卻固 化藉由剝離輥9剝離。薄膜之搬送速度爲1 〇m/min。 然後,在縱延伸裝置1 0中進行縱延伸。 此縱延伸裝置1 0之延伸步驟中,使挾壓後之未延伸 薄膜17在長度方向延伸爲2.0倍。 縱延伸後,橫延伸裝置20使用拉幅器裝置進行橫延 伸,橫延伸時之延伸倍率爲2.0倍。 延伸後之薄膜成爲寬1 3 00的狀態,以切割機切割後 ,使用捲繞裝置60捲繞,製造寬1300mm、膜厚l〇〇#m 、長度l〇〇〇m之實施例1〜8的光學薄膜。 (光學薄膜之評價) 其次’對於實施例1〜8之光學薄膜係以目視觀察光學 薄膜之全區域的表面’觀察薄膜寬方向有無線條狀不均( 橫向不均)。無橫向不均者評價爲等級4、有1條以上未 達3條者評價爲等級3、有3條以上未達6條者評價爲等 級2、有6條以上者評價爲等級1。延遲之均一性評價係-19- 201105480 A suitable UV absorber is a benzotriazole-based UV absorber or a ketone-based UV absorber. It is preferable to add a benzotriazole-based ultraviolet absorber having less unnecessary coloring to the cellulose ester-based resin film. The ultraviolet absorber is added by dissolving the ultraviolet absorber in an organic solvent such as an alcohol or methylene chloride or dioxolane, and then adding it to the dope or directly adding it to the dope composition. If the inorganic powder is not dissolved in an organic solvent, it can be dispersed in an organic solvent and a cellulose ester resin using a dispersing machine or a sand mixer, and then added to the dope. The amount of the ultraviolet absorber to be used is 0.1 to 2 - 5 mass% relative to the mass% of the cellulose ester resin, preferably 〇 5 to 2.0 mass%, more preferably 0.8 to 2 mass%. When the amount of the ultraviolet absorber used exceeds 25 mass%, the transparency of the cellulose vinegar-based resin film tends to be deteriorated. Therefore, the cellulose ester-based resin film is not easy to adhere to each other or to impart slipiness. When using the operation, microparticles can be added as a matting agent. The kind of the microparticles may be an inorganic compound or an organic compound. The fine particles of the inorganic compound are, for example, fine particles such as cerium oxide, titanium oxide, aluminum oxide, zirconium oxide or tin oxide. Among them, a compound containing a ruthenium atom is preferred, and ruthenium dioxide is particularly preferred. The cerium oxide microparticles are, for example, AEROSIL-200, 200V, 300, R972 'R972V, R974, R976, R976S, R202' R812, R805, 0X50, TT600, RY50, RX50, NY50, NAX 50, manufactured by AERO SIL Co., Ltd. NA 5 0 Η, NA 5 0 Y, NX90, RY200S, RY200, RX200, R8200, RA200H, -20- 201105480 RA200HS > NA200Y, R816, R104, RY300, RX300 'R l 06, etc. Among these, from the viewpoint of controlling dispersibility or particle size, AEROSIL-200V and R972V are preferred. The average particle diameter of the fine particles in the film is preferably from 50 nm to 2; / m from the viewpoint of imparting slipperiness and ensuring transparency. It is preferably from 100 nm to 1 OOO nm, more preferably from 100 nm to 500 nm. The average particle size in the film is a photograph of the cross-section of the photograph. In the case of microparticles, the primary particle diameter, the particle diameter after dispersion in a solvent, and the particle diameter after addition to a film often change, and it is important to control the particle size formed by the complex aggregation of the microparticles and the cellulose ester resin in the film. . The amount of the fine particles added is 〇·02 to 0.5% by mass, preferably 0.04 to 0.3% by mass based on the cellulose ester resin film. These additives added to the optical film are applied to the surface of the contact roll, so that the adhesion between the contact roll and the film is less than that of the cooling roll and the film, and the release property of the contact roll and the film can be improved. Fig. 2 is a schematic flow chart showing a first embodiment of an apparatus for carrying out the method for producing an optical film of the present invention by a melt casting film forming method. The embodiment in which the film (melt) initially contacts the surface of the casting roll 5 (Ρ 1 ) is different from the point at which the film contacts the surface of the contact roll (rolling rotating body) 6 (, 2), but sometimes the film is initially in contact with the casting roll. The point ( 51) of the surface of 5 is the same as the point (Ρ2) where the film is in contact with the surface of the contact roll (squeezing rotating body) 6. Further, sometimes the film comes into contact with the contact roller 6 and then comes into contact with the crucible 2. In the present embodiment, a film material containing a resin such as a cellulose resin is mixed - 21 - 201105480, and a resin mixture is obtained, which is then melt-extruded from the casting die 4 onto the casting roll 5 using an extruder 1. The surface of the touch roll 6 was coated with a predetermined amount of the ultraviolet absorber as a release property adjuster 104 by a release agent coating device 1 . The extruded film-like melt is circumscribing the casting roll 5 while the surface of the casting roll 5 is pressed by the contact roller 6 at a predetermined pressure. The rolls circulated to the cooling rolls 7 and 8 in this order were cooled and solidified, and peeled off by the peeling rolls 9. The peeled film 17 is stretched in the longitudinal direction (transport direction) and the lateral direction (width direction) of the film by the longitudinal stretching device 10 and the lateral stretching device 20, and then wound by the winding device 60. The details are as follows. The film-formed thermoplastic resin-containing melt extruded by the casting die 4 is extruded onto a casting roll 5 having a cooling function, and is pressed by the contact roll 6 while being cooled and surface-corrected. The casting roll 5 and the touch roll 6 are not limited to the roll, and may be a drum or a belt or the like. The temperature of the casting roll 5 is preferably set to be lower than the glass transition temperature (Tg) of the resin mixture and above the melting point of the additive. The contact roll 6 is for the film, and the film is pressed by the opposite side of the casting roll 5 in the direction of the casting roll 5. The rotating body of the purpose. The surface of the touch roll 6 is preferably metal and has a thickness of from 1 mm to 10 mm. It is preferably 2 mm to 6 mm. The surface of the rolling rotating body is biased by [] plating, and the surface roughness is preferably 〇·1; ζπι or less, more preferably 0.05/zm or less. The smoother the surface of the roll, the smoother the surface of the resulting film. In the rolling step, the contact roll 6 is preferably composed of an elastic roll (elastic metal roll) having a metal cylinder on its outer periphery. -22- 201105480 In other words, when the pressure of the light 6 is uneven, the film is unevenly distributed. This is orthogonal (Cross Nicols) and becomes uneven brightness. In order to face-correct the film with a uniform pressure, it is preferable to have a contact roller having elasticity of a metal cylinder as described above. The metal material of the surface of the touch roll 6 is required to be smooth and has moderate elasticity and durability. It is preferable to use nickel or the like which is made of carbon steel, stainless steel, titanium, or electroforming. It is preferable to apply a surface treatment such as hard chrome plating, nickel plating, amorphous chromium plating, or ceramic flame spraying, in order to increase the hardness of the surface or to improve the release property from the resin. It is preferable that the surface-processed surface is further honed to become the above-mentioned surface roughness. The contact roller 6 has a double structure of a metal outer cylinder and an inner cylinder, and has a structure in which a cooling fluid flows therebetween and has a space double cylinder. The inner cylinder is made of carbon steel, stainless steel, aluminum, titanium, etc., and the rigid metal inner cylinder is preferable. The inner cylinder is made rigid, and the rotation of the roller can be suppressed. When the inner tube has a tube thickness of 2 to 10 times the outer tube, sufficient rigidity can be obtained. The inner cylinder may be further covered with a resin elastic material such as polyoxane or fluororubber, and the space structure for allowing the cooling fluid to flow may be any one that can uniformly control the surface temperature of the roller, for example, can flow back and forth in the width direction to form a mutual flow. The spiral flow controls the small temperature of the temperature distribution on the surface of the roll. The cooling fluid is not particularly limited, and water or oil can be used in combination with the temperature range. The contact roller 6 is of a Taiko type in which the outer diameter of the center portion is larger than the outer diameter of both end portions. The contact roller generally presses the film at both ends thereof by pressurization means. At this time, since the contact roller is flexible, it has a stronger pressing force at the end portion, and the stronger the pressing, the image is -23-201105480. The roller is set to the Taiko type, and a highly uniform press can be obtained. The diameter of the contact roller 6 is preferably in the range of 200 mm to 500 mm. The effective width of the contact roller 6 must be greater than the film width of the rolling. By the difference between the radius of the central portion of the contact roller 6 and the radius of the end portion (hereinafter referred to as the maximum amount), unevenness in the line or the like occurring in the central portion of the film can be prevented. The highest amount is preferably in the range of 50 to 300 m. The casting rolls 5 and the contact rolls 6 are disposed at opposite sides with respect to the plane of the film to press the film. The casting roll 5 and the touch roll 6 may be in surface contact or in line contact with the film. The surface of the touch roll 6 is coated with a predetermined amount of the release property adjuster 1 〇4 by the release property adjusting agent coating device 100 before the film on the casting roll 5 is pressed. The application of the release modifier 〇4 has been previously described in detail and will be omitted here. In the method for producing an optical film of the present embodiment, the conditions of melt extrusion can be carried out in the same conditions as those used for other thermoplastic resins such as polyester. The material is preferably pre-dried. The water is dried to 100 ppm or less, preferably 200 ppm or less, in a vacuum or a vacuum dryer or a dehumidifying hot air dryer. For example, the cellulose ester-based resin which is dried by hot air or vacuum or under reduced pressure is melted by using the extruder 1 at an extrusion temperature of 200 to 30 CTC, and the foreign matter is removed by filtration using a leaf type filter 2 or the like. When the hopper (not shown) is introduced into the extruder 1, it is preferable to prevent oxidative decomposition or the like under the action of a vacuum or under a reduced pressure or an inert gas atmosphere. When the additive such as a plasticizer is not previously mixed, it can be kneaded on the way of the extruder 24-201105480. In order to allow uniform addition, it is preferred to use a mixing device such as a static mixer 3. The resin such as cellulose resin and other stabilizers which are added as needed are preferably mixed before melting. The mixing may be carried out by a mixer or the like, or may be mixed in a resin preparation process such as a cellulose resin as described above. When using a mixer, a general mixer such as a V-type mixer, a conical spiral type mixer, or a horizontal cylinder type mixer can be used. After the film constituting material is mixed as described above, the mixture is directly melted by using the extruder 1 to form a film. However, once the film constituting material is granulated, the granules may be melt-formed by the extruder 1. Further, when the film constituent material contains a plurality of materials having different melting points, the temperature at which only the material having a lower melting point is melted may be formed. Once the so-called rice porridge-like semi-melt is produced, the semi-melt is introduced into the extruder 1 to form a film. . In the case where the film constituent material contains a material which is easily thermally decomposed, in order to reduce the number of times of melting, it is preferred to form a film without directly forming a film, or a method of forming a film after the above-mentioned rice porridge-like semi-molten. The extruder 1 may use various extruders commercially available, but it is preferably a melt-kneading extruder, and may be a single-shaft extruder or a twin-screw extruder. The pellets are not made of a film-forming material, and when a film is directly formed, since a suitable kneading degree is required, it is preferable to use a twin-screw extruder, and even a single-axis extruder can change the spiral shape to Maddock type, Unimelt type, and Dulmage. The mixing type spiral can be used for moderate mixing. Film constituting material Once a granule or rice porridge semi-melt is used, a single screw extruder or a twin screw extruder can be used. -25- 201105480 The cooling step in the extruder 1 and after the extrusion may be replaced by an inert gas such as nitrogen gas or by reducing the oxygen concentration by pressure reduction. The melting temperature of the film constituent material in the extruder 1 depends on the viscosity or discharge amount of the film constituent material, the thickness of the sheet to be produced, and the like, and thus the preferable conditions are also different 'generally for the glass transition temperature Tg of the film (resin mixture) It is Tg or more and Tg+io〇°c or less, preferably Tg+urc or more and Tg+90°C or less. The melt viscosity at the time of extrusion is from 1 to 100 PaPas, preferably from 10 to 10 00 Pa's. Further, the film forming material in the extruder 1 preferably has a shorter residence time, and is usually within 5 minutes, preferably within 3 minutes, more preferably within 2 minutes. The residence time is affected by the type of the extruder 1 and the extrusion conditions, but the residence time can be shortened by adjusting the supply amount of the material, the L/D, the number of revolutions, the depth of the spiral groove, and the like. The spiral shape or the number of revolutions of the extruder 1 is appropriately selected by the viscosity or discharge amount of the film constituent material. In the present embodiment, the cutting speed of the extruder 1 is from 1/sec to 1 0000/sec, preferably from 5/sec to 1 000/sec, more preferably from 10/sec to 100/sec. The extruder 1 can use a commercially available extruder of a general plastic molding machine. The film constituent material extruded from the extruder 1 is sent to the casting die 4, and is extruded into a film shape by the casting die 4. The molten material discharged from the extruder 1 is supplied to the casting die 4. The casting die 4 is not particularly limited as long as it is used for producing a sheet or a film. The material of the casting die 4 is, for example, sprayed or plated with hard chrome, chromium carbide, chromium nitride, titanium carbide, titanium carbonitride, titanium nitride, ultra-steel, ceramics (tungsten carbide, alumina, chrome oxide). Apply 'and then apply surface finish to polish '1' grinding using the grindstone below #1000 -26- 201105480, using the plane grinding of the diamond grindstone above 000 (the cutting direction is perpendicular to the flow direction of the resin) The processor of electrolytic honing, electrolytic honing, etc., etc. The preferred material of the lip (1 ip) of the casting die 4 is the same as that of the casting die 4. Further, the surface accuracy of the lip sound is preferably 〇 · 5 s or less, more preferably 0.2 S or less. In the present embodiment, the molten resin mixture is extruded into a film-like resin from a casting die 4 installed in an extruder, and then the film-form resin to be extruded is adhered to the casting rolls 5 and the contact rolls 6, and pressurized. After the steps taken. The temperature at which the film-like melt initially contacts the surface of the casting roll 5 and reaches the surface of the contact roller 6 is lowered, preferably within 20 °C. When the temperature at which the film is initially brought into contact with the surface of the casting roll 5 to the surface of the contact roll 6 is too large, the film thickness unevenness is increased due to uneven shrinkage. Further, when the temperature at which the film contacts the touch roll 6 is too low, since the viscosity of the film is high, the correction of the planarity or film thickness unevenness of the film is not sufficient even if the contact roll 6 is narrow. Preferred materials of the casting roll 5 and the contact roll 6 are, for example, carbon steel or stainless steel. The higher the surface precision, the better, and the surface roughness at the maximum height Ry is preferably 0 · 1 / m or less, more preferably 〇. 〇 5 / zm or less. It is preferable that the contact roller 6 presses the film against the casting roll 5 by pressing means. At this time, the line pressure of the contact roller 6 to press the film can be adjusted by a hydraulic piston or the like, preferably from 0.1 to 100 N/mm', more preferably from 1 to 50 N/mm. The casting roll 5 or the contact roll 6 can reduce the diameter of both ends of the roll or have a flexible roll surface in order to improve the adhesion to the film. -27- 201105480 When the portion (the lip portion) of the casting die 4 is decompressed to a portion below the casting roll 5 to 7 OkPa or less, it is found that the above-mentioned mold line has a larger correction effect. Preferably, the pressure is 50 kPa or more and 7 kPa or less. The method of maintaining the pressure of the portion of the casting die 4 from the lip portion of the casting die 4 to 7 OkPa or less is not particularly limited. For example, there is a method in which the casting die 4 is covered with a pressure-resistant member around the roller and pressure-reduced. In this case, the suction device is preferably a measure for heating the heater or the like in order to prevent the device itself from becoming a place where the sublimate is attached. When the suction pressure is too small, there is no way to attract the sublimate, so it is necessary to have an appropriate suction pressure. In the casting die 4, the film-like cellulose ester-based resin in a molten state is adhered to the casting roll 5, the cooling roll 7, and the cooling roll 8 in order, and is cooled and solidified to obtain a cellulose ester-based resin film 17 . In the embodiment of the present invention shown in Fig. 2, the film 17 which has been cooled and solidified by the peeling roller 9 by the cooling roll 8 is introduced into the longitudinal stretching device 1 and is stretched by the roller in the conveying direction (MD direction). Then, the film which has been longitudinally stretched is introduced into a lateral stretching device (tenter) 20' to extend the film 17 in the lateral direction (width direction). By this stretching, the molecules in the film are aligned. After the horizontal extension, the end portion of the film 17 is cut by the width of the product cut by the cutter 19, and then the edge portions of the film are formed by the embossing ring 53 and the back roller 52. Embossing processing (embossing processing), and then winding by the winding device 60 to prevent adhesion or scratching of the optical film (original roll) F. The method of embossing can be performed by having a convex-concave pattern on the side surface. Gold-28- 201105480 is a ring heat or pressure to process. The grip portion of the jig at both ends of the film is usually deformed and cannot be used as a film product, so it is reused as a raw material after being cut. The winding machine to be used can be a general user, and can be wound by a winding method such as a tension method, a fixed torque method, a taper tension method, or a program tension control method in which internal stress is fixed. The step of performing the burring after the lateral stretching and the step of cutting the thick film portion at the end of the film can be performed before the winding step. As described above, the optical film produced in the present embodiment is used as a retardation film, and when the retardation film is used as a polarizing plate protective film, the thickness of the protective film is preferably from 10 to 500 // m. In particular, the lower limit is 20 # m or more, preferably 35 m or more. The upper limit is 150 m or less, preferably 120 m or less. The particularly good range is 35 to 90 // m. When the retardation film is thick, the polarizing plate after the polarizing plate is processed becomes too thick, and it is not suitable for the purpose of thinness and lightness when used for liquid crystal display of a notebook computer or a portable electronic device. Further, when the retardation film is thin, it is difficult to exhibit the retardation of the retardation film, and the moisture permeability of the film is increased, and the function of protecting the polarizer from moisture is lowered, which is not preferable. The optical film of the present invention is a liquid crystal display, a plasma display, an organic EL display, or the like, particularly a functional film for a liquid crystal display, including a polarizing plate protective film, a retardation film, an antireflection film, a brightness enhancement film, and a viewing angle. An optical compensation film or the like is expanded, in particular, a retardation film. ES:} -29-201105480 (Liquid crystal display device) A polarizing plate containing a retardation film composed of the optical film of the present invention has a high display quality as compared with a general polarizing plate, and is particularly suitable for use in a multi-region type. The liquid crystal display device is more preferably used in a multi-region type liquid crystal display device by a birefringence type. Multi-regionalization is also suitable for improving the symmetry of image display. There are various ways of "Maeda, Yamauchi: Liquid Crystal, 6 (3), 303 (2002)". The liquid crystal display unit cell is also described in "Yamada, Yamahara: Liquid Crystal, 7 (2), 184 (2003)", but is not limited thereto. The polarizing plate using the optical film of the present invention can be effectively used for a MVA (Multi-domein Vertical Alignment) type represented by a vertical alignment type, in particular, a MVA type of four divisions, and a known multi-region by electrode arrangement. The PVA (Patterned Vertical Alignment) type, the fusion electrode configuration and the chiral have a large CPA (Continuous Pinwheel Alignment) type. In addition, when it is applied to the OCB (Optical Compensated Bend) type, it is proposed to optically have a biaxial film "T. Miyashita, T. Uchida: J. SID, 3 (1), 29 (1 995 )", by using The polarizing plate of the optical film of the present invention can have a display quality effect. When the display quality effect is exhibited by the polarizing plate using the optical film of the present invention, the arrangement of the liquid crystal type and the polarizing plate is not limited. The display quality of the display unit cell is preferably bilaterally symmetrical when observed by a person. Therefore, when the display unit cell is a liquid crystal display cell, substantially the symmetry of the observation side is prioritized, and the region can be formed into a plurality of regions. The division of the region can be determined by the method known from -30 to 201105480, by considering the properties of the known liquid crystal form by the two-division method and more preferably the four-division method. The liquid crystal display device can also be used as a device for colorization and animation display. 'The optical film of the present invention improves the display quality, and the contrast is improved or the durability of the polarizing plate is improved, so that the eye is not easily fatigued and a faithful moving image can be obtained. display. In the liquid crystal display device, a polarizing plate containing a retardation film composed of the optical film of the present invention is disposed one on the liquid crystal cell, or two sheets are disposed on both sides of the liquid crystal cell. At this time, the retardation film included in the polarizing plate is used in the form of a liquid crystal cell of the liquid crystal display device, which contributes to an improvement in display quality. In the polarizing plate, a polarizing plate protective film of a cellulose derivative is used for the surface opposite to the retardation film from the viewpoint of a polarizer, and a general-purpose TAC film or the like can be used. The polarizing plate protective film located away from the liquid crystal cell side can be provided with other functional layers in order to improve the quality of the display device. The optical film of the present invention can impart antireflection, antiglare, scratch resistance, antifouling adhesion, and brightness enhancement, for example. It can be attached to the surface of the polarizing plate, but is not limited to this. When a retardation film is produced, a functional layer such as an antistatic layer, a hard coat layer, a slippery layer, an adhesive layer, an antiglare layer, and a barrier layer may be applied before and/or after stretching. At this time, various surface treatments such as corona discharge treatment, plasma treatment, and chemical liquid treatment can be performed as necessary. When the optical film of the present invention is used as a retardation film and is used for a protective film of a polarizing plate, the method for producing the polarizing plate is not particularly limited and can be produced by a general method. For example, the obtained retardation film is subjected to alkali treatment, -31 - 201105480, the polyvinyl alcohol film is immersed in an iodine solution, and both sides of the polarizer produced by stretching are completely saponified polyvinyl alcohol aqueous solution, and the polarizing plate is attached to both sides of the polarizer. The method of protecting the film, at least on one side, the retardation film of the polarizing plate protective film of the present invention directly adheres to the polarizer. The easy-adhesion process described in Japanese Laid-Open Patent Publication No. Hei-6-94915, No. Hei 6-118232, and the above-mentioned alkali treatment are carried out, and the polarizing plate processing is carried out. The polarizing plate is composed of a polarizing film and a protective film for protecting both sides thereof, and one surface of the polarizing plate is bonded to the protective film, and the other surface is laminated with the separating film. The protective film and the separator film are used to protect the polarizing plate when the polarizing plate is shipped, and when the product is inspected. At this time, the protective film is bonded to protect the surface of the polarizing plate, and the protective film is used to bond the polarizing plate to the opposite side of the surface of the liquid crystal panel. The separator film is used to protect the adhesive layer attached to the liquid crystal panel, and can be used to bond the polarizing plate to the surface side of the liquid crystal cell. [Embodiment] [Examples] Examples and comparative examples of a method for producing an optical film are shown below. (Examples 1 to 8) (Resin mixture) Cellulose acetate propionate 89% by mass (Ethylene thiol substitution degree: 1.4, propyl thiol substitution degree: 1.35, number average molecular weight: 6 0 0 0 0 -32- 201105480 Trimethylolpropane tribenzoate 9 mass% (plasticizer, melting point 8 51:) (oxidation inhibitor) (IRGANOX XP 420/FD) 0.25 mass% (Ciba Japan) UV absorption 1.6% by mass (TINUVIN 928, manufactured by Ciba Japan, melting point 115 °C) Matting agent (cerium oxide microparticles) 0.15 mass% (seahoster KEP-30: Japan Catalyst Co., Ltd., average particle size 0.3 μηι) Cellulose The thiol substitution degree of the acetate, propionate or the like is determined according to the method specified in ASTM-D8 17-96. After mixing the above materials in a V-type mixer for 30 minutes, a cylindrical pellet having a length of 4 mm and a diameter of 3 mm was melted at 23 CTC under a nitrogen atmosphere using a twin-screw extruder equipped with a strand mold. . The resulting pellet had a glass transition point (Tg) of 1 35 °C. (Production of Optical Film) The above pellets were dried at 100 ° C for 5 hours to have a water content of i 〇〇 ppm, and the pellets were supplied to a single-axis extruder equipped with a T-die 4 as shown in Fig. 2! Film formation is carried out. In the melt, the additive other than the resin contained 11% by mass. The uniaxial extruder 1 system had a spiral diameter of 90 mm and L/D = 30, and the number of revolutions of the spiral was adjusted so that the extrusion amount became 140 kg/h. A nitrogen gas was introduced from the vicinity of the material supply port to -33-201105480 to maintain a nitrogen atmosphere in the extruder 1. The extruder 1 and the T-die 4 were set to a temperature of 240 ° C " Τ 4 4 coat hanger type, width 1500 mm, hard chrome plated on the inner wall, and processed into a mirror surface having a surface roughness of 0. IS. The lip gap of the T die 4 is set to 2 m m. As shown in Fig. 2, the film-like melt extruded from the T-die 4 was dropped on a casting roller 5 having a chrome-plated mirror surface having a surface temperature of 120 ° C and a roll width of 1,600 mm, while being adjusted to a temperature of 120 ° C by the temperature. The contact roller (rolling rotating body) 6 having a roll width of 1600 mm presses the film. On the surface of the contact roller, the P2 position in contact with the melt Y on the casting roll 5 is on the upper side, as shown in Fig. 1, the release modifier is preliminarily coated by the release agent coating device 1 . The mold release modifier coating device 1 is heated to a temperature of 20 ° C at the same temperature as that of the touch roll 6 . The mold release modifier was a copolymer of a UV absorber TIN U V IN 9 2 8 (T - 9 2 8 ) with dimethyl oxa oxide or tetrafluoroethylene. T-928 and dimethyl siloxane are coated in a liquid form, and the tetrafluoroethylene copolymer is coated with 20 parts by mass of 1 part by mass of the solvent xylene. The tetrafluoroethylene copolymer is applied to the surface of the contact roll in a state of being dispersed in a liquid. The coating thickness applied to the contact _ 6 was as shown in Table 1 ' as the production conditions of Examples 1 to 8. The contact angle of the surface of the casting roll 5 with water was 75°. The contact angle of the surface of the contact roll 6 after application of the release agent to the water T-928 was 95. The tetrafluoroethylene copolymer was 109° and the dimethyloxane was 120. ^ The contact roller (squeezing rotary body) 6 presses the film with a linear pressure of 5 N/mm. The casting rolls 5 are made of stainless steel, and the maximum thickness of the surface roughness is -34 - 201105480 0.1 v m or less. The contact roll 6 is a double-tube structure having a metal outer cylinder, an inner cylinder, and a void portion. The material of the metal outer cylinder is stainless steel, and the surface roughness is the maximum height Ry of 0. 〇 5 / zm or less, and the tube thickness is 3 mm. The inner cylinder is made of aluminum and has a cylinder thickness of 30 mm. The gap between the metal outer cylinder and the inner cylinder is 5 mm. The gap portion 47 has oil flowing therein so that the surface temperature of the metal outer cylinder is 120 ° C. The film is pressed against the casting roll 5 and the contact roll (rolling rotating body) 6, and then sequentially connected to the cooling roll 7, and The roll of the cooling roll 8 is solidified by cooling and peeled off by the peeling roll 9. The film transport speed is 1 〇m/min. Then, longitudinal extension is performed in the longitudinal stretching device 10. In the extending step of the longitudinal stretching device 10, the unstretched film 17 after rolling is stretched by 2.0 times in the longitudinal direction. After the longitudinal stretching, the lateral stretching device 20 is transversely stretched using a tenter device, and the stretching magnification at the time of lateral stretching is 2.0 times. The stretched film was in a state of 13,000 in width, and was cut by a cutter, and then wound up by a winding device 60 to produce Examples 1 to 8 having a width of 1300 mm, a film thickness of l〇〇#m, and a length of l〇〇〇m. Optical film. (Evaluation of optical film) Next, the optical film of Examples 1 to 8 was observed by visually observing the surface of the entire region of the optical film. Wireless film-like unevenness (lateral unevenness) was observed in the film width direction. Those who have no horizontal unevenness are evaluated as level 4, those who have one or more than three are evaluated as level 3, those that have three or more are not evaluated as level 2, and those that have six or more are evaluated as level 1. Delayed homogeneity evaluation

[S -35- 201105480 將實施例卜8之薄膜以偏光板之正交下、即直交狀態( cross nicol狀態)所配置的2片偏光子挾著,由其一之偏 光板的外側照射光,由另一之偏光板的外側以目視觀察, 判斷延遲之均一性的等級。光學薄膜之全區域無光透過, 整體均一之暗視野者評價爲等級A、僅部分有線條狀之明 暗者評價爲等級B、部分有線條狀之明暗者評價爲等級C 、部分有明顯線條狀之明暗者評價爲等級D »橫向不均藉 由目視觀察到有6條以上,延遲之不均爲等級D時,製 品品質上有問題。 (比較例1 ) 實施例1之光學薄膜之製造方法中,除了在接觸輥6 之表面未塗佈脫模性調整劑外,與實施例1同樣製作、評 價。 評價結果如表1所示。 (比較例2) 實施例1之光學薄膜之製造方法中,除了在接觸輥6 之表面未塗佈脫模性調整劑,使薄膜狀熔融物掉落前之鑄 造輥5的表面塗佈實施例1所用的脫模性調整劑(T - 9 2 8 )形成0.04 Am之厚度外,與實施例1同樣作製、評價。 201105480 [表1][S-35-201105480 The film of the embodiment 8 is rubbed by two polarizers disposed under the orthogonality of the polarizing plate, that is, in the cross state (cross nicol state), and the light is irradiated from the outside of the polarizing plate. The level of uniformity of the delay is judged by visual observation from the outside of the other polarizing plate. The entire area of the optical film is light-transmissive, and the overall uniform dark field is evaluated as level A, and only part of the line-like light and dark is evaluated as level B, and some lines with light and dark are evaluated as level C, and some are clearly line-shaped. The darkness is evaluated as the grade D. The horizontal unevenness is observed by visual observation. There are 6 or more, and when the delay is not the grade D, there is a problem in the quality of the product. (Comparative Example 1) The method for producing an optical film of Example 1 was produced and evaluated in the same manner as in Example 1 except that the release property adjuster was not applied to the surface of the touch roll 6. The evaluation results are shown in Table 1. (Comparative Example 2) In the method for producing an optical film of Example 1, the surface of the casting roll 5 before the film-like melt was dropped without applying the release property adjusting agent to the surface of the touch roll 6 was applied. The release property adjuster (T-9 2 8 ) used in the above was formed and evaluated in the same manner as in Example 1 except that it was formed to have a thickness of 0.04 Am. 201105480 [Table 1]

脫模性調 整劑 橫向不均結果 延遲不均 種類 厚度(// m) 實施例1 Τ-928 0.04 3 B 實施例2 Τ-928 0.05 4 A 實施例3 Τ-928 0.3 4 A 實施例4 Τ-928 1 4 A 實施例5 Τ-928 1000 4 A 實施例ό Τ-928 1100 3 B 實施例7 四氟化乙烯共聚物 1 2 C 實施例8 二甲基矽氧院 1 3 B 比較例1 Λτττ. Μ - 1 D 比較例2 似鑄造輥塗佈脫模性調整劑塗佈) 1 D 由表1的結果得知藉由在旋轉支持體之表面塗佈脫模 性調整劑,可製作ί黃向不均或延遲不均較少之平面性高的 光學薄膜。此外,由實施例1〜6的結果可知塗佈於旋轉支 持體之表面的脫模性調整劑之厚度在0.〇5~l〇〇〇/zm的範 圍時,橫向不均更 【圖式簡單說明】 [圖1]係使用本發明之光學薄膜之製造方法之流延步 驟與挾壓步驟的槪略圖。 [圖2]係表示本1發明之光學薄膜之製造方法之實施形 態的槪略圖。 【主要元件符號說明】 1 :擠出機 37- 201105480 2 :過濾器 3 :靜態混合機 4 :流延模 5:鑄造輥、旋轉支持體 6:接觸輥、挾壓旋轉體 7、8 :冷卻輕 P1:薄膜最初與鑄造輥表面接觸的點 P2:薄膜與接觸輥表面接觸的點 P3:薄膜離開鑄造輥的點 9 :剝離輥 1 〇 :縱延伸裝置 17 :薄膜 1 9 :切割機 2 〇 :橫延伸裝置 5 2 :背輥 5 3 :浮雕環 60 :捲繞裝置 1〇〇 :脫模性調整劑塗佈裝置 101 :塗佈輥 102 :吸取輥 103 :限制刮板 104 :脫模性調整劑 1 〇 5 :貯存槽 Y :熔融物 -38- 201105480 F :光學薄膜(原捲) -39Release factor lateral unevenness result unevenness type thickness (//m) Example 1 Τ-928 0.04 3 B Example 2 Τ-928 0.05 4 A Example 3 Τ-928 0.3 4 A Example 4 Τ -928 1 4 A Example 5 Τ-928 1000 4 A Example Τ 928-928 1100 3 B Example 7 Tetrafluoroethylene copolymer 1 2 C Example 8 Dimethyl oxime 1 3 B Comparative Example 1 Λτττ. Μ - 1 D Comparative Example 2 Coated casting roll coating release property adjuster coating) 1 D From the results of Table 1, it was found that the release modifier can be applied to the surface of the rotating support to produce ί An optical film having a high degree of flatness with uneven yellowness or less unevenness. Further, from the results of Examples 1 to 6, it is understood that the thickness of the release property adjusting agent applied to the surface of the rotary support is in the range of 0.5 to 5 Å/zm, and the lateral unevenness is more [pattern BRIEF DESCRIPTION OF THE DRAWINGS [Fig. 1] is a schematic view showing a casting step and a rolling step of a method for producing an optical film of the present invention. Fig. 2 is a schematic view showing an embodiment of a method for producing an optical film of the present invention. [Explanation of main component symbols] 1 : Extruder 37 - 201105480 2 : Filter 3 : Static mixer 4 : Casting die 5 : Casting roll, rotating support 6 : Contact roll, rolling rotating body 7, 8 : Cooling Light P1: point P2 at which the film initially contacts the surface of the casting roll: point P3 at which the film contacts the surface of the contact roll: point 9 at which the film leaves the casting roll: peeling roll 1 〇: longitudinal stretching device 17: film 1 9 : cutting machine 2 〇 : Horizontal stretching device 5 2 : Back roller 5 3 : Embossing ring 60 : Winding device 1 : Release agent adjusting device 101 : Coating roller 102 : Suction roller 103 : Restricting blade 104 : Release property Conditioner 1 〇5 : Storage tank Y: melt -38- 201105480 F : Optical film (original roll) -39

Claims (1)

201105480 七、申請專利範圍: 1. 一種光學薄膜之製造方法,其係具備將含有熱可 塑性樹脂之熔融物由流延模擠出成薄膜狀於旋轉支持體表 面的流延步驟、. 將前述流延步驟擠出之薄膜狀的熔融物以前述旋轉支 持體與挾壓旋轉體進行挾壓之挾壓步驟的光學薄膜之製造 方法, 其特徵係在前述挾壓旋轉體表面塗佈使前述挾壓旋轉 體與前述薄膜狀之熔融物之脫模性良好的脫模性調整劑。 2·如申請專利範圍第1項之光學薄膜之製造方法,其 中前述脫模性調整劑含有與前述熔融物所含之添加劑中至 少1種相同的材料。 3·如申請專利範圍第1或2項之光學薄膜之製造方法 ’其中前述脫模性調整劑爲在前述光學薄膜之內部吸收紫 外線用的紫外線吸收劑。 4.如申請專利範圍第i〜3項中任一項之光學薄膜之製 造方法,其中前述脫模性調整劑之沸點爲l5〇〜25(rc。 5·如申請專利範圍第1〜4項中任一項之光學薄膜之製 造方法’其中塗佈前述脫模性調整劑之厚度爲〇〇5〜1〇〇〇 μ m 〇 6.如申請專利範圍第1〜5項中任一項之光學薄膜之製 造方法,其中前述旋轉支持體表面與水的接觸角S1與塗佈 則述脫模性調整劑後之挾壓旋轉體表面與水的接觸角s 2爲 L5°<S2-S1<100°的關係。 -40· 201105480 7 .如申請專利範圍第1〜6項中任一項之光學薄膜之製 造方法,其中前述挾壓旋轉體按壓於前述旋轉支持體之狀 態之前述薄膜狀之熔融物的搬送張力T1與前述挾壓旋轉體 未按壓於前述旋轉支持體之狀態之前述薄膜狀之熔融物的 搬送張力T2之差T1-T2爲1~250N。 8. 如申請專利範圍第1〜7項中任一項之光學薄膜之製 造方法,其中前述熱可塑性樹脂爲纖維素酯系樹脂。 9. —種光學薄膜,其特徵係藉由申請專利範圍第1〜8 項中任一項之光學薄膜之製造方法所製造者。 10. —種光學薄膜之製造裝置,其係具有: 將含有熱可塑性樹脂之熔融物擠出成薄膜狀於旋轉支 持體表面的流延模、 將前述流延模擠出之薄膜狀的熔融物以前述旋轉支持 體與挾壓旋轉體進行挾壓之挾壓手段的光學薄膜之製造裝 置,其特徵係具有在前述挾壓旋轉體表面塗佈使前述挾壓 旋轉體與前述薄膜狀之熔融物之脫模性良好的脫模性調整 劑之脫模性調整劑塗佈裝置。201105480 VII. Patent application scope: 1. A method for producing an optical film, which comprises a casting step of extruding a melt containing a thermoplastic resin into a film form on a surface of a rotating support by a casting die, a method for producing an optical film which is subjected to a rolling step of rolling a film-form melt to be subjected to rolling of the rotating support and the rolling rotating body, and is characterized in that the surface of the rolling rotating body is coated to cause the rolling A mold release property adjuster having a good mold release property between the rotating body and the film-like melt. 2. The method for producing an optical film according to claim 1, wherein the release property adjuster contains at least one of the same materials as the additives contained in the melt. 3. The method for producing an optical film according to claim 1 or 2, wherein the release modifier is an ultraviolet absorber for absorbing ultraviolet rays inside the optical film. 4. The method for producing an optical film according to any one of the above-mentioned claims, wherein the releasing agent has a boiling point of from 15 to 25 (rc. 5) as claimed in claims 1 to 4. The method for producing an optical film according to any one of the preceding claims, wherein the thickness of the release mold adjusting agent is 〇〇5 to 1 〇〇〇μm 〇6, as in any one of claims 1 to 5. A method for producing an optical film, wherein a contact angle S1 between the surface of the rotating support and water and a contact angle s 2 between the surface of the rotating rotating body and the water after coating the releasing agent are L5° < S2 - S1 < The method for producing an optical film according to any one of the first to sixth aspects of the present invention, wherein the rolling rotating body is pressed against the rotating support in the film state. The difference T1 - T2 between the transport tension T1 of the molten material and the transport tension T2 of the film-form melt in a state in which the rolling rotor is not pressed against the rotary support is 1 to 250 N. The method for producing an optical film according to any one of items 1 to 7, wherein The thermoplastic resin is a cellulose ester-based resin. The optical film is produced by the method for producing an optical film according to any one of the first to eighth aspects of the invention. A film manufacturing apparatus comprising: a casting die in which a melt containing a thermoplastic resin is extruded into a film form on a surface of a rotating support; and a film-like melt extruded from the casting die as the rotating support An apparatus for producing an optical film which is a pressing means for rolling a rolling rotating body, characterized in that the surface of the rolling rotating body is coated so that the mold release property of the rolling rotating body and the film-like melt is good. A mold release modifier coating device for a release modifier.
TW099107613A 2009-03-19 2010-03-16 An optical film manufacturing method, an optical film manufacturing method, an optical film manufacturing apparatus TWI522225B (en)

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US7854864B2 (en) * 2006-04-28 2010-12-21 Konica Minolta Opto, Inc. Method for manufacturing an optical film having a convexoconcave structure
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