TW200900224A - Optical sheet manufacture method and optical sheet - Google Patents
Optical sheet manufacture method and optical sheet Download PDFInfo
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- TW200900224A TW200900224A TW97107910A TW97107910A TW200900224A TW 200900224 A TW200900224 A TW 200900224A TW 97107910 A TW97107910 A TW 97107910A TW 97107910 A TW97107910 A TW 97107910A TW 200900224 A TW200900224 A TW 200900224A
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200900224 九、發明說明: 【發明所屬之技術領域】 本發明係關於製造由表面經受軋花處理之非晶態透明結 晶樹脂片製成之光學片的方法。 【先前技術】 已製造出所謂m ’其為表面形成有規則空間幾何形 狀設計(軋花圖案)之樹脂片或薄膜。通常,廣泛使用炼體 擠出法,其中將熱塑性樹脂炼體以薄片形狀擠出τ形模具BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of producing an optical sheet made of an amorphous transparent crystalline resin sheet whose surface is subjected to embossing. [Prior Art] A so-called m' which is a resin sheet or film having a regular space geometry design (embossing pattern) formed on the surface has been produced. Generally, a refining extrusion method in which a thermoplastic resin refining body is extruded in a sheet shape into a tau mold is widely used.
(T -),使在金屬輥(在其圓周表面上具有凹入/凸起形狀) 與橡膠輥之間所夾持及壓縮㈣體冷卻並固化以便連續形 成具有-表面上之凹入/凸起形狀及平坦背表面之薄片⑽ 如,參看日本專利未審查公開案第HEI_9_295346號,專利 文獻1)。 以溶體擠出法’藉由使用同—個具有幾何形狀之實心親 對被擠出T形模具之樹脂同時執行轉印及脫離。為了達成 完美轉印,樹脂必需具有充足熱能,I為了執行脫離,必 而使樹月日冷部至不高於樹脂之玻璃轉移溫度(Tg)。因為溶 體擠出法係藉由使用同—實讀進行轉印及冷卻故難以 執行充分之加熱及冷卻,且難以完美地執行轉印與脫離兩 根據另—軋花片製造方法’將形成於金屬輥或金屬平板 之表面上之軋花圖案轉印至樹脂片之表面。根據另—已知 方法’藉由使用繞在複數個親上且具有形成於環形帶之表 面上之軋花圖案的金屬環形加工帶而在樹脂片之表面上形 126535.doc 200900224 成軋花圖案(例如’參看曰本專利未審查公開案第2001_ 277354號,專利文獻2)。(T -), so that the metal roll (having a concave/convex shape on its circumferential surface) is sandwiched and compressed between the rubber roll and compressed (four) body cooled and solidified to continuously form a concave/convex on the surface A sheet having a shape and a flat back surface (10), for example, Japanese Patent Laid-Open Publication No. HEI_9_295346, Patent Document 1). In the solution extrusion method, transfer and detachment are simultaneously performed by using the same resin having a geometric shape and a solid T-die extruded. In order to achieve perfect transfer, the resin must have sufficient heat energy, and in order to perform the detachment, the cold portion of the tree must be made no higher than the glass transition temperature (Tg) of the resin. Since the solution extrusion method is difficult to perform sufficient heating and cooling by transfer and cooling using the same-real reading, it is difficult to perform transfer and detachment perfectly, and the embossed sheet manufacturing method will be formed in The embossing pattern on the surface of the metal roll or metal plate is transferred to the surface of the resin sheet. According to another known method, a embossed pattern is formed on the surface of the resin sheet by using a metal endless processing belt wound on a plurality of pros and having a embossed pattern formed on the surface of the endless belt. (For example, see Japanese Patent Laid-Open Publication No. 2001-277354, Patent Document 2).
以上文所描述之方式所製造之軋花片可用作(例如)用於 液晶顯示裝置之光學片。特定言之,其中連續安置有三角 形截面形狀之稜柱形狀之稜柱片(prisrn sheet)可用作軋花 片。稜柱片被廣泛稱作亮度改良片(薄膜),用於藉由會聚 背光來改良正面亮度。舉例而言,w〇 2〇〇6/〇71621公開案 (專利文獻3)揭示具有折射率之平面内各向異性且藉由拉伸 在表面上具有棱柱形狀之樹脂片所形成的稜柱片。 【發明内容】 可能需要形成在表面上具有軋花圖案之非晶態樹脂片。 為了使軋花片經受形狀處理以具有折射率之平面内各向異 性,通常沿著單軸方向或雙軸方向拉伸結晶樹脂片。在此 種狀况下,結晶樹脂片較佳處於非晶態下以使得可適當地 以較高精度來執行拉伸製程。 上文所描述之先前技術軋花片製造方法,極難 在使=脂片維持於非晶態下的同時執行㈣處理。亦即, 以先月技術乳花片製造方法,在藉由使溫度上升至高於玻 璃轉移溫度或接近結晶溫度範圍而使樹脂片形成有乾花圖 案之後’不可能防止樹脂在使樹脂片之溫度降至脫離溫度 之冷部製程期間結晶。隨著樹脂片之結晶進行,樹脂變白 Μ㈣度喪失4因此樹脂片變得不適於用作光學片。 古1帛轉印/JB"度較低或脫離溫度較高,則不可能獲得 θ軋花圖案轉印精度。 126535.doc 200900224 a鑒於該等問題,進行本發明。根據本發明之—實施例, 提供月匕夠防止因樹脂片之結晶而變白,同時獲得高精度之 軋花圖案的光學片製造方法。 根據本發明之一實施例’光學片製造方法為由表面經受 規則幾何形狀設計處理之透明熱塑性樹脂片製成之光學片 的製造方法。光學片製造方法包括以下步驟:冑由使用在 表面上形成有幾何形狀設計之金屬環形加工帶在不低於 f 樹脂片之玻璃轉移溫度之溫度下於樹脂片上形成幾何形狀 设計;使形成有幾何形狀設計之樹脂片快速冷卻至低於玻 璃轉移溫度之溫度;及使經快速冷卻之樹脂片自金屬環形 加工帶脫離。 =本發明之—實施例中,在高於樹脂片之玻璃轉移溫度 之溫度下使樹脂片經受幾何形狀設計(軋花形狀)處理,且 此後$樹脂片快速冷卻至低於玻璃轉移溫度或結晶溫度範 —度以抑制樹知片之結晶。亦在本發明之一實施例 中,藉由使用金屬環形加工帶對樹脂片執行札花處理此 後^轉印製程與冷卻製程之間使與金屬環形加王帶組合之 才、ί月日片々彳’且在低於樹脂片之玻璃轉移溫度之溫度下使 樹脂片自金屬環形加工帶脫離。因此,樹脂片之軋花形狀 轉印效能及脫離效能得以改良。 為I防止非晶態樹脂片之結曰曰曰’重點在於在轉印机花形 狀後樹知片至不高於樹脂片之玻璃轉移溫度之溫度的冷卻 速度雖然視用於樹脂>1之材料而定,但是將冷卻速度設 定為(例如)不慢於代/sec且不快於4(rc /sec。若冷卻速度 I26535.doc 200900224 慢於rc/sec,則不可能防止樹腊片之過度結晶,從而導致 變白(喪失透明度)。若將冷卻速度設定為快於4〇t/sec, 則軋花加工降級且變得難以獲得形狀轉印。 當使樹脂片自金屬環形加工帶脫離時,將樹脂片之結晶 度設定為不高於2 0 %且較佳不高於5 %。若樹脂片之:二 超過鳩,則透明度因變白而顯著降減樹脂片變得= 於用作光學片。The embossed sheet produced in the manner described above can be used, for example, as an optical sheet for a liquid crystal display device. Specifically, a prism sheet in which a prism shape having a triangular cross-sectional shape is continuously disposed can be used as the embossed sheet. Prismatic sheets are widely referred to as brightness improving sheets (films) for improving front brightness by concentrating backlights. For example, the publication of WO 2 〇〇 6/〇71621 (Patent Document 3) discloses a prism sheet having an in-plane anisotropy of a refractive index and formed by stretching a resin sheet having a prism shape on the surface. SUMMARY OF THE INVENTION It may be desirable to form an amorphous resin sheet having a embossed pattern on a surface. In order to subject the embossed sheet to a shape treatment to have an in-plane anisotropy of refractive index, the crystalline resin sheet is usually stretched in a uniaxial direction or a biaxial direction. In this case, the crystalline resin sheet is preferably in an amorphous state so that the stretching process can be suitably performed with higher precision. The prior art embossing sheet manufacturing method described above is extremely difficult to perform the (4) treatment while maintaining the =lip sheet in an amorphous state. That is, after the method of manufacturing the pre-monthly technical embossed sheet, after the resin sheet is formed with a dried flower pattern by raising the temperature to a temperature higher than the glass transition temperature or close to the crystallization temperature range, it is impossible to prevent the resin from lowering the temperature of the resin sheet. Crystallization during the cold section process from temperature. As the crystallization of the resin sheet proceeds, the resin becomes white and the degree of 四 (four) is lost. 4 Therefore, the resin sheet becomes unsuitable for use as an optical sheet. If the degree of transfer/JB" is low or the temperature is high, it is impossible to obtain the transfer precision of the θ embossing pattern. 126535.doc 200900224 a The present invention has been made in view of such problems. According to the embodiment of the present invention, there is provided an optical sheet manufacturing method which is capable of preventing whitening due to crystallization of a resin sheet and obtaining a high-precision embossed pattern. According to an embodiment of the present invention, an optical sheet manufacturing method is a method of manufacturing an optical sheet made of a transparent thermoplastic resin sheet whose surface is subjected to a regular geometric design treatment. The optical sheet manufacturing method comprises the steps of: forming a geometric design on a resin sheet at a temperature not lower than a glass transition temperature of the f resin sheet by using a metal annular processing belt having a geometric design formed on the surface; The geometrically designed resin sheet is rapidly cooled to a temperature below the glass transition temperature; and the rapidly cooled resin sheet is detached from the metal endless processing belt. In the embodiment of the invention, the resin sheet is subjected to a geometric design (embossing shape) treatment at a temperature higher than the glass transition temperature of the resin sheet, and thereafter the resin sheet is rapidly cooled to a temperature lower than the glass transition temperature or crystallization. The temperature range is used to suppress the crystallization of the tree. Also in an embodiment of the present invention, the embossing process is performed on the resin sheet by using the metal annular processing belt, and then the metal transfer ring and the cooling process are combined with the metal ring-shaped belt. The resin sheet is detached from the metal endless processing belt at a temperature lower than the glass transition temperature of the resin sheet. Therefore, the embossing shape of the resin sheet is improved in transfer efficiency and release efficiency. In order to prevent the crusting of the amorphous resin sheet, the focus is on the cooling rate at which the temperature of the transfer film is not higher than the glass transition temperature of the resin sheet, although it is used for the resin > Depending on the material, but set the cooling rate to, for example, not slower than generation/sec and not faster than 4 (rc /sec. If the cooling rate I26535.doc 200900224 is slower than rc/sec, it is impossible to prevent excessive waxing Crystallization, resulting in whitening (loss of transparency). If the cooling rate is set to be faster than 4 〇t/sec, the embossing process is degraded and it becomes difficult to obtain shape transfer. When the resin sheet is detached from the metal endless processing belt The crystallinity of the resin sheet is set to not more than 20% and preferably not more than 5%. If the resin sheet: two exceeds 鸠, the transparency is significantly reduced due to whitening, and the resin sheet becomes = used for Optical sheet.
形成於樹脂片之表面上之幾何形狀設計(軋花形狀)並不 受特定限制,而可為具有至少-稜角(尖銳邊緣)之形狀, 諸如稜柱形狀、矩形波形狀及梯形形狀。即使具有至少一 稜角之幸L花形狀仍可以高轉印率來轉印。雖然棱柱形狀之 頂角被設定為(例如)9G。,但是其可為小於%。之銳角或大 於9〇。之鈍角。軋花形狀可為透鏡形狀。 只要樹脂片之材料為透明熱塑性樹脂,其便不受特定限 制。較佳使用PET、卿、此等材料之混合物或共聚物。 1了穩定地保持冷卻速度,可將樹脂片之總厚度設定為 二)500 ’或更薄。軋花形狀高度與樹脂片之總厚度的 率㈣如)9G%或更低1高度比率超過9G%,則在樹 裂痕或其類似物,進而降低處理效能。樹脂片 可為伸長條帶或被切割成預定尺寸之片。 金屬環形加工帶之好粗 '斗可為不鏽鋼、鎳鋼及其類似物。 工帶實施例中,較佳將樹脂片黏附至金屬環形加 行加熱、《及冷卻製程::πτ脂“同時執 中之母一者。作為將樹脂片黏附 126535.doc 200900224 至金屬環形加工帶之方法,例如,存在藉由將金屬環形帶 片加熱至树脂片之軟化溫度(不低於玻璃轉移溫 度之溫度)而使樹脂片緊固地黏附至一帶之方法。以此方 法二可簡化製造設施且可降低製造成本。因為可連續製造 軋化片,故製造效率可得以改良。 在加熱製程期間,例如’加熱係自金屬環形加工帶之内 側開始。藉由自帶之内側開始加熱,可直接加 加熱環形加工帶之片以&自、n ▼之片以改良加熱效率。作為自金屬環形加 工之内侧開始加熱之手段,將帶所纏繞之輥用作加熱觀 去最有效。除上述以外,尚存在藉由提供於親中之電 加熱器來執行加熱之方法或使經加熱之油在輥中循環之方 二:據冷卻手段,冷卻水在金屬輥内部流動。亦可能藉 由輪外加熱器來輔助加熱或藉由空氣流來輔助冷卻。 明之—實施例t,金屬環形加工帶係繞在被設定 低於樹脂片之玻璃轉移:产:的加熱輥及被設定為 加熱輥及冷卻輥之旋轉 τι、 所必需之冷卻速度,根據防止樹脂片之結晶 離及作業㈣π· 冷卻歡溫度、轉間距 令属Speed)(金屬環形加工帶之傳送速度)。 金屬核形加工帶之伞;、 M 面内溫度均一性在很大程度上影塑 欲轉印於樹脂片之表面上 -實祐彻由 上之形狀的加工精度。在本發明之 實施例中,將加熱輥之 〈 對末端部分,且將冷卻輕之中^ 度設定為高於相 相對末端部分。因广分之輥溫度設定為低於 有可能改良金屬環形加工帶之平面 126535.doc -10· 200900224 内溫度均一性及製造具有極佳形態精度之軋花片。 藉由在以面對加熱輥而安置之軋輥與金屬環形加工帶之 間供應樹脂片來對樹脂片執行軋花處理。在此種狀況下, 右金屬環形加工帶與軋輥之間的軋點壓力較低,則軋花形 狀轉印精度降低’而若軋點壓力較高,則軋輥之耐久性受 不利影響且穩定生產變得困難。較佳軋點壓力為不低於5 kg/cm之線壓力且不高於3〇 kg/cm。 若為了提高樹脂片之冷卻速度而提高金屬環形加工帶之 饋送速度’則樹脂片之運動效能變得不穩定或不可獲得充 足預熱,且進而降低饋送效能。環形帶係繞在軋輥及面對 冷卻輥之對置輥上,且樹脂片係藉由被夾持於環形帶與金 屬%形加工帶之間來饋送。因此,有可能改良樹脂片之運 動穩定性及饋送速度。 如上文所描述,根據本發明之光學片製造方法,有可能 以而轉印率在結晶樹脂片之表面上形成所要軋花形狀同時 防止樹脂片因結晶而變白。 【實施方式】 將參看隨附圖式來描述本發明之每一實施例。 [第一實施例] 製造方法之片製造裝置丨的輪廓結構的 圖1為展示用於解釋根據本發明之第一實施例之光學片 圖式。The geometrical design (embossed shape) formed on the surface of the resin sheet is not particularly limited, but may have a shape having at least - an angular (sharp edge) such as a prism shape, a rectangular wave shape, and a trapezoidal shape. Even if it has at least one angular shape, the L-shaped shape can be transferred at a high transfer rate. Although the apex angle of the prism shape is set to, for example, 9G. , but it can be less than %. The acute angle is greater than 9 inches. Obtuse angle. The embossed shape can be a lens shape. As long as the material of the resin sheet is a transparent thermoplastic resin, it is not particularly limited. It is preferred to use PET, qing, a mixture or copolymer of such materials. 1. The cooling rate is stably maintained, and the total thickness of the resin sheet can be set to two) 500 Å or less. The ratio of the height of the embossed shape to the total thickness of the resin sheet (4), for example, 9 G% or less, 1 height ratio exceeding 9 G%, is in the crack of the tree or the like, thereby lowering the treatment efficiency. The resin sheet may be an elongated strip or a sheet cut into a predetermined size. The metal ring processing belt is very thick. The bucket can be stainless steel, nickel steel and the like. In the embodiment of the work belt, it is preferable to adhere the resin sheet to the metal ring-shaped heating, "and the cooling process:: πτ grease" at the same time as the mother of the same. As the resin sheet is adhered to 126535.doc 200900224 to the metal ring processing belt The method, for example, has a method of firmly adhering a resin sheet to a belt by heating the metal endless belt sheet to a softening temperature of the resin sheet (not lower than the temperature of the glass transition temperature). The manufacturing cost can be reduced. Since the rolling sheet can be continuously manufactured, the manufacturing efficiency can be improved. During the heating process, for example, the heating system starts from the inner side of the metal annular processing belt. Heating is started from the inner side of the belt. Directly adding a piece of heated annular processing belt to & n, n ▼ to improve the heating efficiency. As a means of heating from the inside of the metal ring processing, it is most effective to use the wrapped roller as a heating view. In addition, there is a method of performing heating by means of an electric heater provided in the parent or a method of circulating the heated oil in the roller: according to cooling means, cold The water flows inside the metal roll. It is also possible to assist the heating by means of an external heater or to assist the cooling by means of an air flow. In the embodiment t, the metal annular processing belt is wound around a glass set to be lower than the resin sheet: Production: The heating roller and the rotation speed of the heating roller and the cooling roller are set to the necessary cooling speed, according to the prevention of crystallization of the resin sheet and the operation (4) π · cooling temperature, the pitch is Speed) (metal ring processing belt) The conveying speed). The umbrella of the metal core processing belt; M. The in-plane temperature uniformity largely affects the surface to be transferred onto the surface of the resin sheet - the processing precision of the shape of the upper layer is obtained. In an embodiment of the invention, the opposite end portion of the heating roller is set, and the cooling light is set to be higher than the opposite end portion of the phase. The widened roll temperature is set lower than possible to improve the metal annular processing belt. Plane 126535.doc -10· 200900224 Internal temperature uniformity and manufacture of embossed sheets with excellent form accuracy. Supply tree between rolls placed with facing heating rolls and metal endless processing belts The grease sheet is used to perform embossing treatment on the resin sheet. Under such conditions, the nip point pressure between the right metal annular processing belt and the roll is lower, and the embossing shape transfer precision is lowered', and if the nip point pressure is high, Then, the durability of the roll is adversely affected and stable production becomes difficult. The preferred rolling point pressure is a line pressure of not less than 5 kg/cm and not more than 3 〇kg/cm. To increase the cooling rate of the resin sheet. Increasing the feeding speed of the metal endless processing belt', the movement performance of the resin sheet becomes unstable or sufficient preheating is not obtained, and the feeding efficiency is further lowered. The endless belt is wound around the roll and the opposite roller facing the cooling roll, and The resin sheet is fed by being sandwiched between the endless belt and the metal % shaped processing belt. Therefore, it is possible to improve the movement stability and the feeding speed of the resin sheet. As described above, according to the optical sheet manufacturing method of the present invention, it is possible to form a desired embossed shape on the surface of the crystalline resin sheet while the transfer rate is prevented, and to prevent the resin sheet from being whitened by crystallization. [Embodiment] Each embodiment of the present invention will be described with reference to the accompanying drawings. [First Embodiment] Outline structure of a sheet manufacturing apparatus 制造 of a manufacturing method Fig. 1 is a view for explaining an optical sheet pattern according to a first embodiment of the present invention.
1觀12而安置之對置報 片製造裝置 及冷卻輥12、 11而安置之軋 126535.doc 200900224 (背托輥)1 6。 片製造裝置i在乳花帶13與乾輥15之間與札花帶i3同步 也饋达透明非晶形結晶樹脂片1〇,且將樹脂片愿抵著乳花 帶3時藉由加熱輥U將樹脂片加熱至不低於玻璃轉移溫度 又且藉此將軋花帶13之軋花形狀轉印於樹脂片10之 表面上。在樹脂片黏附至軋花帶13之狀態下移動樹脂片 ίο’用冷卻輥12快速冷卻,且使其自乾花帶13脫離以製造 在表面上形成有具有預㈣狀之乳花形狀(稜柱圖案)10a的 透明非晶形結晶樹脂片10。 加熱輥11具有諸如加熱器之内建式加熱構件,且將其表 面溫度設定為高於樹脂片1G之軟化溫度之溫度,亦即高於 樹脂片10之玻璃轉移溫度之溫度。因此,軋花帶13之定位 於加熱輥11上方之部分亦被加熱至此溫度,從而可在此位 置對樹脂片1 0執行加熱製程。 在本實施例中’將加熱輥n之表面溫度設定於不低於 T^g+6(rC且不高於㈣代之溫度範圍内,其中了抑)為樹 月曰片10之玻璃轉移溫度。若所設定溫度低於Tg+6〇c>c ,則 不:獲得軋花圖案至樹脂片10之高轉印精度。若所設定溫 度冋於Tg+90 c且若樹脂片10係由難以維持於非晶態下之 結晶樹脂製成’則樹脂片1〇之結晶過度地加速,且由變白 所引起之透明度降級變得顯著。 冷卻輥12具有諸如水冷卻系統之内建式冷卻構件,且將 其表面溫度設定為低於樹脂片1G之玻璃轉移溫度之溫度。 在本Λ施例中,將冷部親12之表面溫度設定為。因 126535.doc 200900224 此,軋花帶13之定位於冷卻觀 你而可卢… 1視12上方之部分亦得到冷卻, ™立置對樹脂片1 〇執行冷卻製程。 在本實施例中,如圖8A中 τ所不,將加熱輥1丨之中心位詈 之輥溫度設定為高於相對末 & 一 ㈣1刀 另方面,如圖8Β中 所不,將冷卻輥j 2之φ π # $ λ ^ 置之輥溫度設定為低於相對末 知口Ρ刀。因此,故_击丨册 改良軋化π之平面内溫度均—性及製造具 2極佳形態精度之軋花片變為可能。在用於實現此溫度; 之::中’若用於加熱輥"之加熱源係由電加熱器構 則在輥之中心位置處之電線的㈣大於相對輥末端部 分。 加熱輭> 11及冷卻輥12中之至少一去短 V 者經調適成藉由耦接至 諸如馬達之旋轉驅動構件而可旋轉。 軋花帶1靖應Μ具有極佳熱㈣之金屬環形帶製成之 本發明之”金屬環形加工帶"。在本實施例中軋花帶13係 由錄鋼製成且在其表面上具有其中連續排列有三角形截面 形狀之凹槽(稜柱形狀)之軋花形狀(幾何形狀設計)⑴。棱 柱頂角並不受特定限制’且其較佳可為(例如)120。或更 小、及90。。軋花帶13較佳為無縫的(無接面)。軋花帶較佳 透過藉由在於内表面侧具有軋花形狀之管狀樹脂母版上電 成形來生長鎳鋼或透過繞在輥上且直接執行精度切割處理 來形成’但本發明並不僅限於此等方法。 在本實施例中,將軋花形狀13a之延伸方向(隆脊方向)設 定為樹脂片iO之寬度方向(橫向方向(TD)),但方向並不限 於此,且可為樹脂片1〇之運動方向(機器方向(md))。為了 126535.doc -13· 200900224 改良與樹脂片1之可脫離性,可將脫模劑塗佈於關於軋花 帶13之上面形成軋花形狀⑴之表面上。脫模劑較佳為含 氟樹脂、含矽樹脂或其類似物。 軋花形狀13a並不限於三角形截面形狀(棱柱形狀)。棱柱 形狀之頂角並不限於如圖从中所示之9〇。,頂角可為如圖 9B中所示之小於9〇。之銳角,或如圖9C中所示之大於9〇〇之 鈍角。軋花形狀13a可為如圖9£>中所示之矩形波(脈衝波) 形狀’或如圖9E中所示之梯形形狀。甚至可以高轉印率將 形狀形成為上文所描述之具有至少一稜角(尖銳邊緣)之軋 花形狀。 軋花形狀可為各種透鏡形狀。透鏡形狀可為圓柱形狀或 陣列形狀。透鏡表面可為諸如球形表面或非球形表面之曲 面形狀,或並不限於連續曲面形狀之由複數個曲面形狀構 成之複合形狀。 提供軋輥15以便與軋花帶13合作之輥夾持並壓縮樹脂片 ίο且將軋花帶13之表面上之軋花形狀13a轉印至樹脂片 之表面。在本實施例中,如類似於加熱輥u,軋輥15具有 内建式加熱源且具有作為輔助輥自背面加熱軋花帶13上之 樹脂片10的功能。雖然軋輥15之圓周表面為平坦光滑表 面,但是預定軋花形狀可形成於軋輥丨5之圓周表面上以使 得形狀能夠轉印至樹脂片10之背面。軋輥15可為具有冷卻 機制之冷卻輥以便辅助背面之脫離且防止背面輥(代犯 之形狀之轉印。 由軋輥15及軋花帶13施加於樹脂片1〇之軋點壓力大幅影 I26535.doc 14 200900224 響軋铯形狀13a至樹脂片丨〇之轉印精度。在本實施例中, 將軋點壓力設定為5 kg/cmt更高及3〇 kg/cm或更低之線壓 力。若軋點壓力低於5 kg/cm,則軋花形狀13a至樹脂片1〇 之轉印精度降低,而若軋點壓力超過30 kg/cm,則軋輥15 及軋花帶13之耐久性受不利影響且穩定生產變得困難。1 and 12, the opposite side of the sheet manufacturing apparatus and the cooling rolls 12, 11 are placed and rolled 126535.doc 200900224 (back roller) 16. The sheet manufacturing apparatus i feeds the transparent amorphous crystalline resin sheet 1同步 in synchronization with the zigzag belt i3 between the nipple belt 13 and the dry roll 15, and the resin sheet is pressed against the nipple belt 3 by the heating roller U. The resin sheet is heated to not lower than the glass transition temperature and thereby the embossed shape of the embossed belt 13 is transferred onto the surface of the resin sheet 10. The resin sheet is moved rapidly by the cooling roll 12 in a state where the resin sheet is adhered to the embossed belt 13, and is detached from the dried flower ribbon 13 to produce an embossed shape having a pre- (four) shape on the surface (prism pattern) A transparent amorphous crystalline resin sheet 10 of 10a. The heating roller 11 has a built-in heating member such as a heater, and its surface temperature is set to a temperature higher than the softening temperature of the resin sheet 1G, that is, a temperature higher than the glass transition temperature of the resin sheet 10. Therefore, the portion of the embossed belt 13 positioned above the heating roller 11 is also heated to this temperature, so that the heating process can be performed on the resin sheet 10 at this position. In the present embodiment, 'the surface temperature of the heating roller n is set to be not lower than T^g+6 (rC and not higher than the temperature range of (four), and the suppression is) the glass transition temperature of the tree slab 10 . If the set temperature is lower than Tg + 6 〇 c > c, no: high transfer precision of the embossed pattern to the resin sheet 10 is obtained. If the set temperature is less than Tg + 90 c and the resin sheet 10 is made of a crystalline resin which is difficult to maintain in an amorphous state, the crystal of the resin sheet 1 is excessively accelerated, and the transparency caused by whitening is degraded. Become remarkable. The cooling roll 12 has a built-in cooling member such as a water cooling system, and its surface temperature is set to a temperature lower than the glass transition temperature of the resin sheet 1G. In the present embodiment, the surface temperature of the cold portion 12 is set to be. Because of 126535.doc 200900224, the position of the embossed belt 13 is on the cooling view. You can also cool the part of the upper part of the 12th 12, and the TM is placed on the resin sheet 1 〇 to perform a cooling process. In the present embodiment, as shown in FIG. 8A, the temperature of the roller at the center of the heating roller 1 is set higher than that of the opposite end. One (four) and the other, as shown in FIG. 8A, the cooling roller is used. The roll temperature of j 2 φ π # $ λ ^ is set lower than that of the opposite end boring tool. Therefore, it is possible to improve the in-plane temperature uniformity of rolling π and to manufacture embossed sheets having excellent shape accuracy. The heating source used to achieve this temperature is: if the heating source is used, the electric heater is constructed by the electric heater at the center of the roller (4) larger than the opposite roller end portion. At least one of the heated crucible > 11 and the chill roll 12 is adapted to be rotatable by being coupled to a rotary drive member such as a motor. The embossed belt 1 is a "metal endless processing belt" of the present invention which is made of a metal endless belt having excellent heat (4). In the present embodiment, the embossed belt 13 is made of recorded steel and is on the surface thereof. A knurled shape (geometric design) (1) having a groove (prism shape) in which a triangular sectional shape is continuously arranged. The apex angle of the prism is not particularly limited' and it may preferably be, for example, 120 or less. And 90. The embossed belt 13 is preferably seamless (no joint). The embossed belt is preferably grown by electroforming the tubular resin master having a embossed shape on the inner surface side to grow nickel steel or through The method is formed by winding on a roll and directly performing precision cutting processing. However, the present invention is not limited to such a method. In the present embodiment, the extending direction (ridge direction) of the embossed shape 13a is set to the width direction of the resin sheet iO. (lateral direction (TD)), but the direction is not limited thereto, and may be the direction of movement of the resin sheet 1 (machine direction (md)). For the improvement of the detachability of the resin sheet 1 for 126535.doc -13· 200900224 Applying a release agent to the embossed belt 13 The surface is formed on the surface of the embossed shape (1). The release agent is preferably a fluorine-containing resin, a ruthenium-containing resin or the like. The embossed shape 13a is not limited to a triangular cross-sectional shape (prism shape). The apex angle of the prism shape is not It is limited to 9 如图 as shown in the figure. The apex angle may be an acute angle of less than 9 〇 as shown in Fig. 9B, or an obtuse angle of more than 9 如图 as shown in Fig. 9C. The embossed shape 13a may be A rectangular wave (pulse wave) shape as shown in Fig. 9 or a trapezoidal shape as shown in Fig. 9E. The shape can be formed even at a high transfer rate to have at least one angular shape as described above (sharp The embossed shape of the edge. The embossed shape may be various lens shapes. The lens shape may be a cylindrical shape or an array shape. The lens surface may be a curved shape such as a spherical surface or an aspherical surface, or is not limited to a continuous curved shape. A composite shape composed of a plurality of curved shapes. A roll 15 is provided to sandwich and compress the resin sheet with the roll engaged with the embossed belt 13 and transfer the embossed shape 13a on the surface of the embossed belt 13 to the surface of the resin sheet. In this embodiment For example, similar to the heating roller u, the roller 15 has a built-in heating source and has a function as an auxiliary roller for heating the resin sheet 10 on the embossed belt 13 from the back. Although the circumferential surface of the roller 15 is a flat smooth surface, it is predetermined The embossed shape may be formed on the circumferential surface of the roll crucible 5 so that the shape can be transferred to the back surface of the resin sheet 10. The roll 15 may be a cooling roll having a cooling mechanism to assist the detachment of the back surface and prevent the back side roll (the shape of the reverse roll) The transfer pressure of the embossing point pressure applied to the resin sheet 1 by the roll 15 and the embossed belt 13 is greatly improved. In the present embodiment, the transfer precision of the shape 13a to the resin sheet 响 is obtained. The nip pressure was set to a higher line pressure of 5 kg/cmt and a pressure of 3 〇kg/cm or less. If the nip point pressure is less than 5 kg/cm, the transfer precision of the embossed shape 13a to the resin sheet 1 降低 is lowered, and if the nip point pressure exceeds 30 kg/cm, the durability of the roll 15 and the embossed belt 13 is affected. Adverse effects and stable production become difficult.
女裝對置輥16作為附加輥,此輥可在樹脂片丨〇自冷卻輥 12上之軋花▼ 13脫離時使用。如類似於冷卻輥12,對置輥 16具有内建式冷卻構件以維持類似於冷卻輥12之溫度之表 面溫度且具備自背面冷卻樹脂片1〇之功能。對置輥“之圓 周表面具有平坦光滑表^由對置親丨6及軋花帶1 3施加於 樹脂)no之軋點壓力並不受特定限制,但使對置輥16之圓 周表面緊密接觸樹脂片1G之背表面的礼點壓力即足夠。 只要樹脂片10之材料為透明熱塑性結晶樹脂,其便不受 特定限制。在本實施例中,使用聚對苯二曱酸乙二醇酯 (PET)、聚萘二甲酸乙二醇s§(pEN)、此等材料之混合物或 共聚物’其為在用於維持非晶態之冷卻製程期間經受異常 嚴格製造條件之結晶樹脂。本實施例採用以伸長條帶形狀 形成非晶態樹脂片1〇且將其連續饋送至片製造裝置1之方 法。或者’可採用將被切割成預定尺寸之樹脂片ι〇連續地 逐個饋送至片製造裝置丨之方法。 此處,非晶態之樹脂片10意謂(例如)3%或更小之結晶 率。本實施例之片製造裝置】執行藉由使用乳花帶13 = 晶態樹脂片10之表面乾花且快速冷卻樹脂片之製程以製造 具有地或更小、或較佳或更小之結晶率之非晶態樹 126535.doc 15 200900224 脂片(軋花片或稜柱片)10。若結晶率超過2〇%,則由變白 所引起之透明度降級變得顯著且樹脂片變得不適於用作光 學片。 右結晶率超過2〇%,則材料之揚氏模數(Young's m〇dulUS)通常會變高。因此,若使經受軋花處理之樹脂片 在此後經受拉伸處理,則拉伸所需之負載變大且需要將拉 伸期間之加熱溫度設定為較高。若尤其藉由拉伸製程使樹 脂片具有雙折射率且若樹脂片在拉伸之前具有超過2〇%之 結晶率,則所要雙折射率難以獲得。 為了在於樹脂片10上處理軋花形狀 < 前及之後維持樹脂 片10之非晶態,樹脂片10之冷卻速度[〇c/sec]變為在自在 加熱輥11上對樹脂片1〇之形狀轉印至在冷卻輥12上樹脂片 10之脫離的週期期間的重要問題。雖然視樹脂片1〇之材料 而定,但是冷卻速度較佳設定為不慢於5<t/sec&不快於 40°C/Sec,且更佳設定為不慢於1{rc/sec且不快於 30°C/Sec。若冷卻速度慢於5°C/Sec,則不可能防止樹脂片 之過度結晶,從而導致變白(喪失透明度)。若將冷卻速度 設定為快於40°C/seC,則軋花加工降級且獲得極佳形態轉 印變得困難。藉由實現上文所描述之範圍内之冷卻速=, 在藉由片製造裝置1來執行軋花形狀轉印製程之前及之後 將樹脂片之結晶率之增量抑制於5%或更小變為可能。亦 可能將自乳花帶脫離之樹脂片之結晶率抑制於2 或更 小 ° 為了實現樹脂月10之冷卻速度,片製造裝置丨具有在加 126535.doc - 16- 200900224 熱輥11與冷卻輥12之間的規定輥間距離、環形帶13之饋送 速度、樹脂片10相對於冷卻輥12之接觸角及其類似物。可 提高複數個冷卻輥12 ^ 若輥11與12之間的距離過遠,則必需增加環形帶13之饋 送速度以確保冷卻速度。然而,隨著環形帶13之饋送速度 增大’樹脂片1 〇之運動穩定性降低。因此,變得難以預期The women's opposite roller 16 serves as an additional roller which can be used when the resin sheet is detached from the embossing ▼ 13 on the cooling roller 12. Like the cooling roller 12, the opposing roller 16 has a built-in cooling member to maintain a surface temperature similar to the temperature of the cooling roller 12 and has a function of cooling the resin sheet 1 from the back surface. The nip pressure of the opposing roller "the circumferential surface has a flat smooth surface ^ applied by the opposing relative 6 and the embossed tape 13 to the resin" no is not particularly limited, but the circumferential surface of the opposing roller 16 is in close contact The point pressure of the back surface of the resin sheet 1G is sufficient. The material of the resin sheet 10 is not particularly limited as long as it is a transparent thermoplastic crystalline resin. In the present embodiment, polyethylene terephthalate ( PET), polyethylene naphthalate s§ (pEN), a mixture or copolymer of such materials' which is a crystalline resin which is subjected to abnormally strict manufacturing conditions during a cooling process for maintaining an amorphous state. A method of forming an amorphous resin sheet 1 in an elongated strip shape and continuously feeding it to the sheet manufacturing apparatus 1. Alternatively, 'the resin sheet ι which is cut into a predetermined size may be continuously fed one by one to the sheet manufacturing apparatus. Here, the amorphous resin sheet 10 means a crystallization ratio of, for example, 3% or less. The sheet manufacturing apparatus of the present embodiment is performed by using the umrim tape 13 = crystalline resin sheet 10 Dry flowers on the surface and rapidly cool the resin a process for producing an amorphous tree 126535.doc 15 200900224 fat sheet (embossed sheet or prism sheet) having a crystallization ratio of ground or smaller, or preferably smaller or smaller. If the crystallization ratio exceeds 2%, The deterioration of transparency caused by whitening becomes remarkable and the resin sheet becomes unsuitable for use as an optical sheet. When the right crystallization ratio exceeds 2%, the Young's m〇dulUS of the material generally becomes high. If the resin sheet subjected to the embossing treatment is subjected to the stretching treatment thereafter, the load required for the stretching becomes large and the heating temperature during the stretching is required to be set high. If the resin sheet is especially made by the stretching process It has a birefringence and if the resin sheet has a crystallinity of more than 2% by weight before stretching, the desired birefringence is difficult to obtain. In order to process the embossed shape on the resin sheet 10, the resin sheet 10 is maintained before and after. In the crystalline state, the cooling rate [〇c/sec] of the resin sheet 10 becomes an important problem during the period in which the shape of the resin sheet 1 is transferred from the heating roller 11 to the detachment of the resin sheet 10 on the cooling roll 12. Although depending on the material of the resin sheet, it is However, the speed is preferably set to be no slower than 5 < t / sec & not faster than 40 ° C / Sec, and more preferably set to be no slower than 1 {rc / sec and not faster than 30 ° C / Sec. If the cooling rate is slower than At 5 ° C / Sec, it is impossible to prevent excessive crystallization of the resin sheet, resulting in whitening (loss of transparency). If the cooling rate is set to be faster than 40 ° C / se C, the embossing process is degraded and an excellent morphology is obtained. Printing becomes difficult. By achieving the cooling rate in the range described above, the increase in the crystallinity of the resin sheet is suppressed to 5 before and after the embossing shape transfer process is performed by the sheet manufacturing apparatus 1. % or less becomes possible. It is also possible to suppress the crystallization rate of the resin sheet from the emulsified belt to 2 or less. In order to achieve the cooling rate of the resin month 10, the sheet manufacturing apparatus has a weight of 126535.doc - 16 - 200900224 The prescribed inter-roller distance between the heat roller 11 and the cooling roller 12, the feed speed of the endless belt 13, the contact angle of the resin sheet 10 with respect to the cooling roller 12, and the like. The plurality of cooling rolls 12 can be raised. If the distance between the rolls 11 and 12 is too far, it is necessary to increase the feed speed of the endless belt 13 to ensure the cooling rate. However, as the feeding speed of the endless belt 13 is increased, the movement stability of the resin sheet 1 降低 is lowered. So it becomes hard to anticipate
穩定生產率或預熱變得不足且轉印效能降低。若輥丨丨與U 之間的距離過近,則環形帶13之熱交換變得不足,且因此 難以在所要溫度下對樹脂片1 〇執行加熱及冷卻製程。 在一較佳實例中,當將加熱輥u之溫度設定為不低於Stable productivity or preheating becomes insufficient and transfer efficiency is lowered. If the distance between the rolls U and U is too close, the heat exchange of the endless belt 13 becomes insufficient, and thus it is difficult to perform the heating and cooling process on the resin sheet 1 at a desired temperature. In a preferred embodiment, when the temperature of the heating roller u is set to be not lower than
Tg+60°C且不高於Tg+90°C時,當將冷卻輥12之溫度設定為 3〇°C且將環形帶13之饋送速度設定為5 m/min時,將加熱 輥11與冷卻輥12之間的輥間距離設定為不短於丨〇〇 mm且不 長於400 mm。此輥間距離視樹脂片丨〇之材料而變化。舉例 而言,輥間距離對於PET而言不短於1〇〇 mm且不長於2〇〇 mm且對於PEN而言不短於100 mm且不長於4〇〇 。 100 mm之輥間距離在5 m/min下對應於2〇。〇/3“之冷卻速 度,且4〇〇 mm之輥間距離對應於5°C/sec之冷卻速度。 顯然可藉由改變軋花帶1 3之饋送速度同時使輥丨丨與j 2 之間的距離保m ^來獲得必要冷卻速纟。在此種狀況 下’在輥11與12之間800 _之距離下,較佳饋送速度為不 慢於5 m/min且不快於1〇 m/min。 為了 L疋地保持冷卻條4牛,較佳將樹脂片! 〇之總厚度設 疋為500 μηι或更薄。軋花形狀之高度與樹脂片⑺之總厚度 126535.doc -17- 200900224 的比率較佳為90%或更古 t 右回度比率超過90〇/〇,則在樹 月曰片中引起裂痕或其類似物,且處理效能降低。 接下來’將對使用如上述所建構之片製造裝置ι之本實 施例之光學片製造方法進行描述。 將預设至供應輥(未展示)之非晶態樹脂片i 〇供應於札花 帶13與軋輥15之間。接著,在加熱輥η上將樹脂片ίο加埶 至龍於破璃轉移溫度或更高之溫度,且將其夾持及屢縮 '花帶1 3與軋輥1 5之間以將軋花帶1 3之軋花形狀13 a轉 印於樹脂片1 〇之表面上。 —將被轉印札花形狀之樹脂片_定至軋花帶13且連同軋 化帶13起朝向冷卻輥12饋送。在冷卻輥12上將樹脂片1〇 連同軋花帶13-起冷卻至低於玻璃轉移溫度之溫度。在此 V卻製程期間’在轉印軋花形狀之後,使樹脂片⑺以維持 非晶態之冷卻速度快速冷卻。使經冷卻之樹脂片10在經過 軋化帶13與對置輥16之間的軋點後自軋花帶13脫離,繞在 纏繞輥(未展示)上。 以此方式,製造在表面上形成有軋花形狀i〇a之非晶態 树知片10。藉由使用如上述所建構之片製造裝置1,使樹 月曰片10經受軋花處理使得可簡化製造設施以達成成本降 低因為可連續製造軋花片’故製造效率可得以改良。 在本實施例中’在對應於玻璃轉移溫度或更高之溫度下 十樹月曰片1 0執行軋花處理,且此後使樹脂片快速冷卻至低 於玻璃轉移溫度之溫度。因此,有可能維持非晶態同時抑 制树月曰片1 0之結晶。此外,藉由使用軋花帶1 3對樹脂片10 126535.doc -18· 200900224 執行軋花處理,在轉印製程與冷卻製程之間的時期期間使 樹月曰片ίο與軋花帶13共同冷卻,且在低於樹脂片之玻璃轉 移狐度之溫度下使樹脂片10自軋花帶13脫離。因此,關於 樹脂片10之軋花形狀轉印效能及脫離效能可得以改良。 ,根據本實施例,可以高轉印率在片表面上形成所要軋花 形狀同時抑制由非晶態結晶樹脂片10之結晶所引起之變 白。特定言之’在本實施例中,可以98%或更高之高轉印 率將軋花形狀轉印至樹脂片i 〇。 本說明書中將轉印率定義如下。亦即,如圖2八請中 所示’轉印率㈤係由(H2/H1)X1(H)表示,其中叫示形成 於樹脂片10上之亲丨冗;并J灿古ώ ’阿度且H1表示形成於軋花帶13上 之軋花形狀高度。 本發明之發明者量測了藉由使用具有以5G_距所安 置頂角90。之截面為等腰三 使用炫體擠出型《之… 的母版、藉由 乳花方= 及本發明之使用層壓型式之 軋化方法的樹脂片的實際軋花 ψ。掘-7也 里〜、,·°果展不於圖3 揭不了與熔體擠出型式相比,層壓 率形成軋花形狀。 J 呵轉印 軋花帶13之平面内溫度均一 樹脂片之矣而… f在很大耘度上影響形成於 術月曰片之表面上之形狀的加工精度 熱輥11之中心邛八之趣.w ώ 實施例t,將加 您十“。P刀之輥溫度設定為高於相 將冷卻輥!2之中心部分末Μ分’且 分。因此,有可处改Μ 低於相對末端部 有可此改良軋花帶13之平面 造具有極佳形態精度之軋花片。 夂二—性及製 126535.doc -19- 200900224 成= = = :式形成有軋花形狀之樹脂一 性心光學 具有沿著料方向之隆脊方之㈣片10的結構。 著⑨含方向之稜柱圖案(軋花形狀)1〇3沿 月向以預定間距連續排列於樹脂片H>之表面上。樹 月曰片1〇可在此狀態下用作液晶顯Μ置之稜柱片。 Γ 右^著稜柱隆脊方向(χ軸方向)以預定拉伸速率來拉伸 =4中所示之樹脂片1〇,則可改變片光學特性。亦即,可 二程而在沿著Χ軸方向之平面内折射率(ηΧ) 思、轴方向之平面内折射率㈣之間形成折射率差 拉伸裊%可適當地且以高精度被執行,因為樹脂片1 〇 係處於具有2〇%或更小之結晶率之非晶態下。 在本實知例中,將具有沿著拉伸方向之大折射率之樹脂 材料(諸如ΡΕΤ及ΡΕΝ)用作樹脂片1〇之材料,且藉由拉伸 製程使樹脂片10具有nx>ny之折射率各向異性。如上述所 建,之樹脂片10具有沿著棱柱陣列方向之偏光成份之輸出 光置大於沿著稜柱延伸方向之偏光成份之輸出光量的光學 特f因為/σ著稜柱隆脊方向(x軸方向)之偏光成份具有 因在稜柱傾斜表面處在臨界角反射下重複發生全反射而返 回至,入射側之光置’其大於關於輸出光之棱柱形成表面 之/口著稜柱陣列方向(γ軸方向)的偏光成份。 曰圖5—為展示使用具有作為棱柱片之結構之樹脂片1〇之液 a曰顯示裝置20的結構的示意性圖式。液晶顯示裝置具有 液,,肩示面板2 1、將液晶顯示面板2丨夾在中間之第一偏光 126535.doc -20 - 200900224 器22A及第一偏光器22B、棱柱片ι〇、漫射片η及背光單 元24。 /堯柱片10對應於藉由片製造裝置1而形成有軋花形狀之 樹月曰片1 G ’且被用作用於改良液晶顯示裝置之正面亮度 之免度改良薄膜。稜柱片W安置於用於將來自背光單元24 之照明光(背光)漫射及輸出之漫射片23之光輸出側,且且 有將來自漫射片23之輸出光會聚至正面方向的功能。、 —一對將液晶顯示面板21夾在中間之偏光器22八及22b經 安置以使其透射軸線"a"及"b,,變成正交。在所示實例中, 稜柱片係以使得稜柱片1〇之稜柱排列方向(¥轴方向)變 成大致平行於定位於背光單元24之側之第一偏光器ΜΑ之 透射軸線"a”的方式而安置。當使用沿著稜柱隆脊方向 軸方向)所拉伸之棱柱片10時,此實例尤其有效。因為具 有大輸出光量之偏光成份可有效地進入液晶顯示面板21, 故正面亮度可得以改良。 稜柱片10並不限於單一稜柱片結構,而可層壓複數個稜 柱片。在此種狀況下,較佳在使得各別稜柱片之隆脊方向 垂直於彼此的同時層壓稜柱片。 (第二實施例) 接下來,將描述本發明之第二實施例。圖6為展示第二 實施例之片製造裝置2之結構的示意性圖式。在圖6中藉 由使用相同參考符號來表示對應於第一實施例之元件的元 件’省去了其詳細描述。 在第二實施例之片製造裝置2中,金屬環形帶14繞在軋 126535.doc •21 - 200900224 輥15及面對樹脂片10之背面(不形成札花形狀之面)之對置 輥16上。樹脂片Π)在自樹u1G之加熱/轉印製程至冷卻/ 脫離製程之時期期間被夹持及I缩於軋花帶13與環形们4 之間。 雖然環形帶係由諸如鎳鋼之金屬製成,但是材料並不 限於金屬,而可使用諸如耐熱pET之耐熱樹脂。環形帶Μ 之表面為鏡面表面。若必需,則可形成一形狀以使得該形 狀可轉印及形成至樹脂片1 0之背表面。 雖然視材料而定,但是環形帶14之厚度較佳不薄於3〇 μΓη且不厚於1000 μπι。若厚度超過1〇〇〇 μηι,則不可能將 環形帶繞在加熱輥及冷卻輥上。若厚度薄於3〇 pm,^可 能在饋送樹脂片10期間引起翹曲或引起裂痕而造成強度方 面之問題。 在如上述所建構之第二實施例之片製造裝置^中,在自 樹脂片10之加熱/轉印製程至冷卻/脫離製程之時間週期期 間在將樹脂片夾持及固持於軋花帶13與環形帶14之間的狀 態下輸送樹脂片10。因此’有可能改良樹脂片1〇之運動穩 定性以使得可藉由加快饋送迷度來改良用於防止由樹脂片 10之結晶所引起之變白之冷卻速度的設定靈活性。 根據第二實施例’藉由對環形帶14之表面執行軋花處理 且在其上形成軋花形狀,不僅可在樹脂片10之正表面上而 且可在背表面上以高轉印精度形成軋花形狀。 (第三實施例) 圖7說明藉由使用片製造裝置2藉由使兩個樹脂片i〇s及 126535.doc •22- 200900224 lot熱結合來製造層壓片1〇L。在此實例中,雖然軋花形狀 係藉由軋花帶13而轉印至樹脂片i〇s之表面,但是兩個樹 脂片10s及lot被夾持及壓縮於軋花帶13與環形帶14之間以 被熱結合且整合在一起。因此,有可能易於製造具有形成 於表面上之預定軋花形狀之層壓片1〇L。 兩個樹脂片10s及10t係被一起饋送至片製造裝置樹 脂片l〇s及10t可由同一類型之樹脂片製成或可包括不同類 型之樹脂片。此外,可同時饋送三或三個以上樹脂片。 [實例] 將描述本發明之實例’但本發明並不僅限於該等實例。 (實例1) 藉由T形模具擠出法形成200 μπι厚度之非晶形pET片 (Tg :約75°〇。將非晶形PET片饋送至片製造裝置1或2, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90。之等腰三角形之稜柱的稜柱片。 [製造條件] 片材料:非晶形PET 厚度:200 μπι 稜柱間距:50 μηι 加熱輥11之表面溫度:150°C 軋輥15之表面溫度:50°C 冷卻輥12之表面溫度:30°C 對置輥16之表面溫度:30°C 樹脂片之冷卻速度:20°C /sec 126535.doc • 23- 200900224 (片饋送速度:5 m/min) 加熱報11與軋輥丨5之間的軋點線壓力:1 5 kg/cm (實例2) 藉由丁开’模具擠出法形成200 μηι厚度之非晶形pen片 (Tg :約120°C)。將非晶形PEN片饋送至片製造裝置工或2, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90。之等腰三角形之稜柱的稜柱片。 [製造條件] Γ 片材料:非晶形pen 厚度:200 pm 稜柱間距:1〇〇 μηι 加熱輥u之表面溫度:190°C 軋輥15之表面溫度:70°C 冷卻輥12之表面溫度:30t: 對置輥16之表面溫度:30°C f 樹脂片之冷卻速度:10°C/sec 、 (片饋送速度:3 m/min) 加熱輥11與軋輥15之間的軋點線壓力:l5kg/em (實例3) m 藉由T形模具擠出法形成2〇〇 厚度 rT 又〈非晶形PEN片When Tg + 60 ° C and not higher than Tg + 90 ° C, when the temperature of the cooling roll 12 is set to 3 ° C and the feed speed of the endless belt 13 is set to 5 m / min, the heating roll 11 is The distance between the rolls between the cooling rolls 12 is set to be not shorter than 丨〇〇mm and not longer than 400 mm. The distance between the rolls varies depending on the material of the resin sheet. For example, the distance between rolls is not shorter than 1 mm and not longer than 2 mm for PET and not shorter than 100 mm for PEN and no longer than 4 inches. The distance between the rolls of 100 mm corresponds to 2 inches at 5 m/min. 〇/3" cooling rate, and the distance between rolls of 4 mm corresponds to a cooling rate of 5 ° C / sec. Obviously by changing the feeding speed of the embossing belt 13 while making the roll and j 2 The distance between the two is guaranteed to obtain the necessary cooling speed. In this case, the distance between the rolls 11 and 12 is preferably no slower than 5 m/min and not faster than 1 〇m. /min. In order to keep the cooling strip 4 cows L, it is preferable to set the total thickness of the resin sheet to 500 μηι or less. The height of the embossed shape and the total thickness of the resin sheet (7) 126535.doc -17- The ratio of 200900224 is preferably 90% or more t. The right-return ratio exceeds 90 〇/〇, causing cracks or the like in the tree sap, and the treatment efficiency is lowered. Next, the use will be as described above. The optical sheet manufacturing method of the present embodiment is described. The amorphous resin sheet i 预设 preset to the supply roller (not shown) is supplied between the zigzag belt 13 and the roll 15. Next, On the heating roller η, the resin sheet ίο is twisted to a temperature at which the dragon is transferred to the glass or higher, and is clamped and Between the shrinking strip 1 3 and the roll 15 5, the embossed shape 13 a of the embossed strip 13 is transferred onto the surface of the resin sheet 1 - the resin sheet to which the zigzag shape is transferred is set to The embossed belt 13 is fed along with the tempering strip 13 toward the chill roll 12. The resin sheet 1 〇 is cooled on the chill roll 12 together with the embossed strip 13 to a temperature below the glass transition temperature. 'After transferring the embossed shape, the resin sheet (7) is rapidly cooled at a cooling rate maintaining the amorphous state. The cooled resin sheet 10 is self-rolled after passing through a rolling point between the rolling belt 13 and the opposite roller 16. The flower strip 13 is detached and wound around a winding roller (not shown). In this manner, an amorphous tree 10 having a embossed shape i 〇 a formed on the surface is manufactured by using the sheet constructed as described above. The apparatus 1 is subjected to embossing treatment of the saplings 10 so that the manufacturing facility can be simplified to achieve cost reduction because the embossing sheets can be continuously produced, so that the manufacturing efficiency can be improved. In the present embodiment, 'corresponding to the glass transition temperature or At a higher temperature, the ten tree moon smear 10 performs embossing treatment, and thereafter the resin is made. It is rapidly cooled to a temperature lower than the glass transition temperature. Therefore, it is possible to maintain the amorphous state while suppressing the crystallization of the sapphire film 10. Further, by using the embossing tape 13 to the resin sheet 10 126535.doc -18· 200900224 The embossing process is performed, and the tree slab ίο is co-cooled with the embossed belt 13 during the period between the transfer process and the cooling process, and the resin sheet 10 is made at a temperature lower than the glass transition degree of the resin sheet. Therefore, the embossing shape transfer performance and the detachment efficiency with respect to the resin sheet 10 can be improved. According to the present embodiment, the desired embossed shape can be formed on the sheet surface at a high transfer rate while suppressing The whitening caused by the crystallization of the amorphous crystalline resin sheet 10. Specifically, in the present embodiment, the embossed shape can be transferred to the resin sheet i 可以 at a high transfer rate of 98% or more. The transfer rate is defined in the present specification as follows. That is, as shown in FIG. 2, the 'transfer rate (five) is represented by (H2/H1) X1 (H), wherein the relatives formed on the resin sheet 10 are verbosely redundant; and J Canku's And H1 represents the height of the embossing shape formed on the embossed belt 13. The inventors of the present invention measured the apex angle 90 by 5G_ by using. The cross-section is an isosceles three. The actual embossing of the resin sheet using the spheroidal extrusion type "...", by the embossing side = and the lamination method using the lamination type of the present invention. Digging -7 also ~,, · ° fruit exhibition is not as shown in Figure 3 reveals that the lamination rate forms a embossed shape compared to the melt extrusion pattern. J The transfer embossed belt 13 has a uniform temperature in the plane of the resin sheet... f affects the processing precision of the shape formed on the surface of the sapphire slab on a large degree of twist. .w 实施 Example t, will add you ten. The temperature of the P-roller is set higher than the phase of the center of the cooling roller! 2, and the points are divided. Therefore, there is a change in the lower than the opposite end. There is a embossed sheet which can be improved in the plane of the embossed belt 13 and has excellent form precision. 夂二—性和制126535.doc -19- 200900224 成== = : Forming a resin-shaped heart with a embossed shape The structure of the (four) sheet 10 having the ridges along the direction of the material is provided. The prism pattern (the embossed shape) of the ninth direction is successively arranged on the surface of the resin sheet H> at a predetermined pitch in the moon direction. The ruthenium sheet 1 can be used as a prism sheet of a liquid crystal display in this state. 右 The right side of the prism ridge direction (the z-axis direction) is stretched at a predetermined stretching rate = the resin sheet 1 shown in Fig. 4 〇, the optical properties of the sheet can be changed. That is, the refractive index (ηΧ) in the plane along the x-axis can be two-way, and the axis The formation of the refractive index difference between the in-plane refractive index (four) and the stretching % can be suitably and with high precision because the resin sheet 1 is in an amorphous state having a crystallinity of 2% or less. In the present embodiment, a resin material having a large refractive index in the stretching direction (such as tantalum and niobium) is used as the material of the resin sheet 1 , and the resin sheet 10 has nx >ny by a stretching process. The refractive index anisotropy. As described above, the resin sheet 10 has an optical output of the polarizing component along the prism array direction, and an optical specificity of the output light amount of the polarizing component along the extending direction of the prism. The polarization component of the ridge direction (x-axis direction) has a repetitive total reflection under the critical angle reflection at the inclined surface of the prism, and the incident side light is set to be larger than the prism-forming surface of the output light. The polarizing component of the prism array direction (γ-axis direction). FIG. 5 is a schematic view showing the structure of a liquid-display device 20 using a resin sheet having a structure as a prism sheet. The liquid crystal display device has , the shoulder panel 2 1 , the first polarized light 126535.doc -20 - 200900224 22A and the first polarizer 22B, the prism sheet ι〇, the diffusion sheet η and the backlight unit 24 sandwiching the liquid crystal display panel 2 The cymbal sheet 10 corresponds to the embossed tree slab 1 G ' formed by the sheet manufacturing apparatus 1 and is used as a modified film for improving the front luminance of the liquid crystal display device. It is used for the light output side of the diffusion sheet 23 for diffusing and outputting the illumination light (backlight) from the backlight unit 24, and has a function of condensing the output light from the diffusion sheet 23 to the front direction. The polarizers 22 and 22b sandwiching the liquid crystal display panel 21 are disposed such that their transmission axes "a" and "b become orthogonal. In the illustrated example, the prism sheet is such that the prism column arrangement direction (the ¥ axis direction) becomes substantially parallel to the transmission axis "a" of the first polarizer 定位 positioned on the side of the backlight unit 24 This example is particularly effective when the prism sheet 10 stretched along the direction of the axis of the prism ridge is used. Since the polarizing component having a large output light amount can effectively enter the liquid crystal display panel 21, the front luminance can be obtained. The prism sheet 10 is not limited to a single prism sheet structure, but a plurality of prism sheets may be laminated. In this case, it is preferred to laminate the prism sheets while the ridge directions of the respective prism sheets are perpendicular to each other. (Second Embodiment) Next, a second embodiment of the present invention will be described. Fig. 6 is a schematic view showing the structure of the sheet manufacturing apparatus 2 of the second embodiment. By using the same reference symbols in Fig. 6 The detailed description of the elements corresponding to the elements of the first embodiment is omitted. In the sheet manufacturing apparatus 2 of the second embodiment, the metal endless belt 14 is wound around a roll 126535.doc • 21 - 200900224 roll 15 And a facing roller 16 facing the back surface of the resin sheet 10 (the surface on which the zigzag shape is not formed). The resin sheet is held during the period from the heating/transfer process to the cooling/disengaging process of the tree u1G and I is contracted between the embossed belt 13 and the ring 4. Although the endless belt is made of a metal such as nickel steel, the material is not limited to metal, and a heat resistant resin such as heat resistant pET may be used. a mirror surface. If necessary, a shape may be formed such that the shape may be transferred and formed to the back surface of the resin sheet 10. Although depending on the material, the thickness of the endless belt 14 is preferably not less than 3 〇 μΓ and It is not thicker than 1000 μm. If the thickness exceeds 1 μm, it is impossible to wind the endless belt around the heating roller and the cooling roller. If the thickness is thinner than 3 μm, it may cause warpage during feeding of the resin sheet 10 or A problem arises in that the crack is caused to cause a strength. In the sheet manufacturing apparatus of the second embodiment constructed as described above, the resin sheet is subjected to a period of time from the heating/transfer process of the resin sheet 10 to the cooling/disengaging process. Clamping and holding on the embossed belt 13 The resin sheet 10 is conveyed in a state between the endless belts 14. Therefore, it is possible to improve the kinematic stability of the resin sheet 1 so that the change caused by the crystallization of the resin sheet 10 can be improved by accelerating the feeding density. Setting flexibility of the cooling rate of white. According to the second embodiment, by performing embossing on the surface of the endless belt 14 and forming a embossed shape thereon, not only on the front surface of the resin sheet 10 but also on the back The embossed shape is formed on the surface with high transfer precision. (Third Embodiment) FIG. 7 illustrates the thermal bonding of two resin sheets i〇s and 126535.doc •22-200900224 lot by using the sheet manufacturing apparatus 2 A laminate 1〇L was produced. In this example, although the embossed shape was transferred to the surface of the resin sheet i〇s by the embossed tape 13, the two resin sheets 10s and lot were clamped and compressed. The embossed belt 13 and the endless belt 14 are thermally bonded and integrated. Therefore, it is possible to easily manufacture the laminate 1L having a predetermined embossing shape formed on the surface. The two resin sheets 10s and 10t are fed together to the sheet manufacturing apparatus. The resin sheets 10s and 10t may be made of the same type of resin sheet or may include different types of resin sheets. Further, three or more resin sheets may be fed simultaneously. [Examples] Examples of the invention will be described, but the invention is not limited to the examples. (Example 1) An amorphous pET sheet having a thickness of 200 μm was formed by a T-die extrusion method (Tg: about 75° 〇. The amorphous PET sheet was fed to the sheet manufacturing apparatus 1 or 2, and was produced under the following conditions. A plurality of prism sheets arranged in an array on the surface of the sheet at an apex angle of 90. The sheet material of the isosceles triangle prism. [Production conditions] Sheet material: amorphous PET Thickness: 200 μπι Prism spacing: 50 μηι Surface temperature of the heating roller 11: 150 ° C Surface temperature of roll 15: 50 ° C Surface temperature of cooling roll 12: 30 ° C Surface temperature of opposing roll 16: 30 ° C Cooling rate of resin sheet: 20 ° C / sec 126535.doc • 23- 200900224 (Piece feed speed: 5 m/min) The line pressure between the heating report 11 and the roll 丨5: 15 kg/cm (Example 2) The thickness of 200 μηι was formed by Dingkai's die extrusion method. Crystalline pen sheet (Tg: about 120 ° C.) The amorphous PEN sheet is fed to a sheet manufacturing apparatus or 2, and is manufactured under the following conditions with a plurality of vertices 90 arranged in an array on the surface of the sheet. Prismatic prism of triangular prism. [Manufacturing conditions] Γ Sheet material: amorphous pen Thickness: 200 pm Column spacing: 1 〇〇μηι Surface temperature of the heating roll u: 190 ° C Surface temperature of the roll 15: 70 ° C Surface temperature of the cooling roll 12: 30 t: Surface temperature of the opposing roll 16: 30 ° C f Resin sheet Cooling rate: 10 ° C / sec, (sheet feeding speed: 3 m / min) Rolling line pressure between the heating roller 11 and the roll 15: l5 kg / em (Example 3) m formed by T-die extrusion method 2〇〇 thickness rT and <amorphous PEN film
Ug .約120。〇。將非晶形PEN片饋送至片 衣造裝置1或2 , 且在以下條件下製造具有許多個以陣列形 LTlfeon。 卜列於片表面 上頂角90之等腰三角形之稜柱的稜柱片。 [製造條件] 126535.dc), -24- 200900224 片材料:非晶形PEN 厚度.2 0 〇 pm 棱柱間距.300 μιη 加熱輥11之表面溫度:190°C 軋輥1 5之表面溫度:7〇。〇 冷卻輥12之表面溫度:3〇。〇 對置輥16之表面溫度:30°C 樹脂片之冷卻速度:l〇°C/sec ( ' (片饋送速度:3 m/min) 加熱輥11與軋輥15之間的軋點線壓力:15 kg/cm (實例4) 藉由T形模具擠出法形成200 μιη厚度之非晶形pen片 (Tg:約12〇。〇。將非晶形PEN片饋送至片製造裝置1或2, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90°之等腰三角形之稜柱的稜柱片。 [製造條件]Ug. About 120. Hey. The amorphous PEN sheet was fed to the sheet forming apparatus 1 or 2, and manufactured in a number of arrays of LTlfeon under the following conditions. A prismatic sheet of prismatic prisms with an apex angle of 90 on the surface of the sheet. [Manufacturing conditions] 126535.dc), -24- 200900224 Sheet material: Amorphous PEN Thickness. 2 0 〇 pm Prismatic pitch. 300 μιη Surface temperature of the heating roller 11: 190 ° C Surface temperature of the roll 15: 7 Torr.表面 Surface temperature of the chill roll 12: 3 〇. The surface temperature of the 〇 opposed roller 16: 30 ° C The cooling rate of the resin sheet: l 〇 ° C / sec ( ' (sheet feeding speed: 3 m / min) The line pressure between the heating roller 11 and the roller 15: 15 kg/cm (Example 4) An amorphous pen piece having a thickness of 200 μm was formed by a T-die extrusion method (Tg: about 12 Å. 非晶. The amorphous PEN sheet was fed to the sheet manufacturing apparatus 1 or 2, and A prism sheet having a plurality of prisms of an isosceles triangle arranged in an array on the surface of the sheet at an apex angle of 90° was produced under the following conditions. [Manufacturing conditions]
I 片材料:非晶形PEN 厚度:200 pm 棱柱間距· 1 〇 μηιI Sheet material: Amorphous PEN Thickness: 200 pm Prism spacing · 1 〇 μηι
• 加熱輥丨1之表面溫度:190°C 軋輥15之表面溫度·· 7〇°c 冷卻輥12之表面溫度:30°C 對置親16之表面溫度:3 0 °C 樹脂片之冷卻速度:1 〇°C /sec 126535.doc -25- 200900224 (片饋送速度:3 m/min) 加熱輥11與軋輥15之間的軋點線壓力:15kg/cm (實例5) 藉由T形模具擠出法形成5〇〇 4以厚度之非晶形吒τ片 (Tg :約75。〇。將非晶形pET片饋送至片製造裝置丨或2, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90。之等腰三角形稜柱的稜柱片。 [製造條件]• Surface temperature of heating roll :1: 190°C Surface temperature of roll 15··7〇°c Surface temperature of chill roll 12: 30°C Surface temperature of set 亲16: 30 °C Cooling rate of resin sheet :1 〇°C /sec 126535.doc -25- 200900224 (Piece feed speed: 3 m/min) The nip line pressure between the heating roller 11 and the roll 15: 15 kg/cm (Example 5) by T-die The extrusion method forms an amorphous 吒τ sheet having a thickness of 5 〇〇 4 (Tg: about 75 Å. The amorphous pET sheet is fed to the sheet manufacturing apparatus 丨 or 2, and is manufactured in a plurality of arrays under the following conditions. A prism sheet of an isosceles triangular prism arranged on the surface of the sheet at an apex angle of 90. [Manufacturing conditions]
f 片材料:非晶形PET 厚度.500 μι^ 稜柱間距:100 μηι 加熱輥11之表面溫度:15〇。〇 軋輥1 5之表面溫度:5 〇 冷卻輥12之表面溫度:3〇。〇 對置輥16之表面溫度:30°C 樹脂片之冷卻速度:15°C/sec k (片饋送速度:5 m/min) 加熱輥π與軋輥15之間的軋點線壓力:15kg/cm (實例6) 藉由T形模具擠出法形成20 μιη厚度之非晶形ρΕτ片 (Tg :約75°〇。將非晶形PET片饋送至片製造裝置is:, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90°之等腰三角形之稜柱的稜柱片。 [製造條件] 126535.doc -26 - 200900224f sheet material: amorphous PET thickness. 500 μιη prism spacing: 100 μηι The surface temperature of the heating roller 11: 15 〇.表面 Surface temperature of the roll 15: 5 表面 Surface temperature of the cooling roll 12: 3 〇. The surface temperature of the 〇 opposed roller 16: 30 ° C The cooling rate of the resin sheet: 15 ° C / sec k (sheet feeding speed: 5 m / min) The line pressure between the heating roller π and the roll 15: 15 kg / Cm (Example 6) An amorphous ρΕτ sheet having a thickness of 20 μm was formed by a T-die extrusion method (Tg: about 75° 〇. The amorphous PET sheet was fed to a sheet manufacturing apparatus is: and manufactured under the following conditions) A plurality of prismatic prisms arranged in an array on the surface of the sheet having an equilateral triangle of 90° apex angle. [Manufacturing conditions] 126535.doc -26 - 200900224
片材料:非晶形PET 厚度.20 μηι 棱柱間距:20 μπιSheet material: Amorphous PET Thickness. 20 μηι Prismatic spacing: 20 μπι
加熱輥11之表面溫度:15〇°CSurface temperature of heating roller 11: 15 〇 ° C
軋輥15之表面溫度:5(TC • 冷卻輥12之表面溫度:3(TC 對置輥16之表面溫度:30°C 樹脂片之冷卻速度:30°C/sec Γ) (片饋送速度:5 m/min) 加熱輥11與軋輥15之間的軋點線壓力:30 kg/cm (實例7) 藉由T形模具擠出法形成200 μιη厚度之非晶形pen片 (Tg:約120。〇。將非晶形PEN片饋送至片製造裝置^2, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90。之等腰三角形之稜柱的稜柱片。 [製造條件] { 片材料:非晶形PEN 厚度:200 μιη 稜柱間距:50 μηι • 加熱輥11之表面溫度:200°C 軋輥15之表面溫度·· 70°C 冷卻輥12之表面溫度:50°C 對置輥16之表面溫度:50°C 樹脂片之冷卻速度:40°C /sec 126535.doc -27- 200900224 (片饋送速度:5 m/min) 3〇 kg/cm 加熱輥11與軋輥15之間的軋點線壓力 (實例8) 藉由T㈣具擠出法形成15G师厚度之非晶形咖片 g.約120〇。將非晶形PEN片饋送至片製造裝置_, 且在以下條件下製造具有許多個㈣列形式排列於片表面 上頂角90。之等腰三角形之稜柱的稜柱片。 [製造條件]Surface temperature of the roll 15: 5 (TC • Surface temperature of the cooling roll 12: 3 (surface temperature of the TC counter roller 16: 30 ° C cooling rate of the resin sheet: 30 ° C / sec Γ) (sheet feed speed: 5 m/min) Line pressure between the heating roll 11 and the roll 15: 30 kg/cm (Example 7) An amorphous pen piece having a thickness of 200 μm was formed by a T-die extrusion method (Tg: about 120. The amorphous PEN sheet is fed to the sheet manufacturing apparatus 2, and a prism sheet having a plurality of prisms of an isosceles triangle arranged in an array on the surface of the sheet at an apex angle 90 is fabricated under the following conditions. [Manufacturing conditions] { Sheet material: Amorphous PEN Thickness: 200 μη Prism pitch: 50 μηι • Surface temperature of the heating roller 11: 200 ° C Surface temperature of the roll 15 · 70 ° C Surface temperature of the cooling roll 12: 50 ° C Opposite roll 16 Surface temperature: 50 ° C Cooling speed of resin sheet: 40 ° C / sec 126535.doc -27 - 200900224 (sheet feeding speed: 5 m / min) 3 〇 kg / cm Rolling between the heating roller 11 and the roll 15 Dotline pressure (Example 8) An amorphous coffee wafer of 15G thickness was formed by T (four) extrusion method. About 120 Å. Amorphous PEN sheets were fed to the sheet. _ Manufacturing apparatus and manufacturing [Manufacturing conditions] (iv) having a plurality of columns are arranged in the form of an isosceles triangle the apex angle of the prism sheet 90. The upper surface of the prism sheet. Under the following conditions
片材料:非晶形PEN 厚度:15 0 μηι 稜柱間距:1〇〇 μιη 加熱輥11之表面溫度:1 8 〇。〇 軋輥1 5之表面溫度:7 〇 冷卻輥12之表面溫度:3〇°c 對置輥16之表面溫度:3〇。〇 樹脂片之冷卻速度:3〇°C/sec (片饋送速度:5 m/min) 加熱輥11與軋輥15之間的軋點線壓力:3t)kg/cni (實例9) 藉由T形模具擠出法形成200 μιη厚度之非晶形pEN片 (Tg :約120°〇。將非晶形PEN片饋送至片製造裝置, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90。之等腰三角形之稜柱的稜柱片。 [製造條件] 126535.doc -28- 200900224Sheet material: Amorphous PEN Thickness: 15 0 μηι Prismatic spacing: 1 〇〇 μιη Surface temperature of the heating roller 11: 1 8 〇.表面 Surface temperature of the roll 15: 7 表面 Surface temperature of the cooling roll 12: 3 〇 ° c Surface temperature of the opposing roll 16: 3 Torr. Cooling rate of the resin sheet: 3 ° C / sec (sheet feeding speed: 5 m / min) The line pressure between the heating roller 11 and the roll 15: 3 t) kg / cni (Example 9) by T shape The die extrusion method forms an amorphous pEN sheet having a thickness of 200 μm (Tg: about 120° 〇. The amorphous PEN sheet is fed to a sheet manufacturing apparatus, and is manufactured under the following conditions with a plurality of arrays arranged on the surface of the sheet. Angle 90. The prismatic piece of the prism of the isosceles triangle. [Manufacturing conditions] 126535.doc -28- 200900224
片材料:非晶形PEN 厚度:200 μιη 棱柱間距:350 μιη 加熱輥11之表面溫度:190°C 軋輥15之表面溫度:70°C . 冷卻親1 2之表面溫度:3 0 °C 對置輥16之表面溫度:30°C 樹脂片之冷卻速度:l〇°C/sec ί; (片饋送速度:3 m/m in) 加熱輥11與軋輥1 5之間的軋點線壓力:1 5 kg/cm (實例10) 藉由T形模具擠出法形成300 μιη厚度之非晶形pen片 (Tg :約120°C)。將非晶形PEN片饋送至片製造裝置1或2, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90°之等腰三角形之稜柱的稜柱片。 [製造條件]Sheet material: Amorphous PEN Thickness: 200 μη Prism spacing: 350 μη Surface temperature of heating roll 11: 190 °C Surface temperature of roll 15: 70 ° C. Surface temperature of cooling pro 1 2: 30 °C opposed roll Surface temperature of 16: 30 ° C Cooling speed of resin sheet: l 〇 ° C / sec ί; (sheet feeding speed: 3 m / m in) nip line pressure between heating roller 11 and roller 15: 1 5 Kg/cm (Example 10) An amorphous pen piece (Tg: about 120 ° C) having a thickness of 300 μm was formed by a T-die extrusion method. The amorphous PEN sheet was fed to the sheet manufacturing apparatus 1 or 2, and a prism sheet having a plurality of prismatic prisms arranged in an array on the surface of the sheet having an apex angle of 90° was fabricated under the following conditions. [Manufacture conditions]
^ 片材料:非晶形PEN 厚度:300 μιη 稜柱間距:75 μιη 加熱輥11之表面溫度:190°C 軋輥15之表面溫度:7〇°c 冷卻輥12之表面溫度:30°C 對置輥16之表面溫度:30°C 樹脂片之冷卻速度:l〇°C/sec 126535.doc •29- 200900224 (片饋送速度:4 m/min) 加熱輥11與軋輥15之間的軋點線壓力:5 kg/cm (實例11) 藉由T形模具擠出法形成300 μηι厚度之非晶形pet片 (Tg :約75°〇。將非晶形PET片饋送至片製造裝置1或2, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90。之等腰三角形之稜柱的稜柱片。 [製造條件]^ Sheet material: Amorphous PEN Thickness: 300 μη Prism spacing: 75 μη Surface temperature of the heating roller 11: 190 ° C Surface temperature of the roll 15: 7 ° ° C Surface temperature of the cooling roll 12: 30 ° C Opposite roll 16 Surface temperature: 30 ° C Cooling speed of resin sheet: l 〇 ° C / sec 126535. doc • 29 - 200900224 (sheet feeding speed: 4 m / min) The line pressure between the heating roller 11 and the roller 15: 5 kg/cm (Example 11) An amorphous pet piece having a thickness of 300 μm was formed by a T-die extrusion method (Tg: about 75° 〇. The amorphous PET sheet was fed to the sheet manufacturing apparatus 1 or 2, and below Under the conditions, a prism sheet having a plurality of prisms of an isosceles triangle arranged in an array on the surface of the apex angle 90 is fabricated. [Manufacturing conditions]
Γ 片材料:非晶形PET 厚度:100 μηι 棱柱間距· 1 〇〇 pm 加熱輥11之表面溫度:150°C 軋報1 5之表面溫度:5 0 °C 冷卻輥12之表面溫度:30°C 對置輥16之表面溫度:30°C 樹脂片之冷卻速度:251:/sec ^ (片饋送速度:5 m/min) 加熱親11與軋輥丨5之間的軋點線壓力:5 kg/em (實例12) 藉由T形模具擠出法形成10〇 厚度 τ又 < 非晶形pET片 (Tg :約75°C)。將非晶形PET片饋送至片製 教造裝置1戋2, 且在以下條件下製造具有許多個以陣列形 I- TI ^ Λ挪列於片表面 上頂角90之4腰三角形之稜柱的稜柱片。 [製造條件] 126535.doc -30- 200900224 片材料:非晶形PET 厚度.10 0 μηι 稜柱間距:1〇〇 μιη 加熱輥11之表面溫度:15〇。〇 軋輥15之表面溫度:50°c 冷卻輥12之表面溫度:30°C 對置輥16之表面溫度:30〇C 樹脂片之冷卻速度:6°C/sec (片饋送速度:2 m/min) 加熱輥11與軋輥1 5之間的軋點線壓力:20 kg/cm (實例13) 藉由Τ形模具擠出法形成300 μηι厚度之非晶形PEN片 (Tg :約120°〇。將非晶形PEN片饋送至片製造裝置1或2, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90。之等腰三角形之稜柱的稜柱片。 [製造條件] 片材料:非晶形pen 厚度:300 μιη 棱柱間距:50 μηι 加熱輥11之表面溫度:190°C 軋輥1 5之表面溫度:8 〇 冷卻輥12之表面溫度:6(TC 對置輥16之表面溫度:60°C 樹脂片之冷卻速度:5 °C /sec 126535.doc • 31 - 200900224 (片饋送速度:3 m/min) 加熱輥11與軋輥15之間的軋點線壓力:20 kg/cm (比較實例1) 藉由T形模具擠出法形成200 μιη厚度之非晶形pet片 (Tg :約75°C)。將非晶形PET片饋送至片製造裝置1或2, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90。之等腰三角形之稜柱的稜柱片。 [製造條件] 片材料:非晶形PET 厚度:200 μιη 稜柱間距:100 μιη 加熱輥11之表面溫度:170°C 軋輥1 5之表面溫度:4〇°C 冷卻輥12之表面溫度:30°C 對置輥16之表面溫度:3 (TC 樹脂片之冷卻速度:3t:/sec I’ (片饋送速度:4 m/min) 加熱輥11與軋輥1 5之間的軋點線壓力:1 5 kg/em (比較實例2) 藉由τ形模具擠出法形成200 μηι厚度之非晶形pEN片 (Tg :約12〇。〇。將非晶形pEN片饋送至片製造裝置1或2, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90。之等腰三角形之稜柱的稜柱片。 [製造條件] 126535.doc • 32- 200900224Γ Sheet material: Amorphous PET Thickness: 100 μηι Prism spacing · 1 〇〇pm Surface temperature of heating roller 11: 150 ° C Rolling surface temperature of 15 5: 50 °C Surface temperature of cooling roll 12: 30 ° C Surface temperature of the opposing roller 16: 30 ° C Cooling speed of the resin sheet: 251: / sec ^ (sheet feeding speed: 5 m / min) Heating line pressure between the pro-11 and the roll 丨 5: 5 kg / Em (Example 12) A 10 〇 thickness τ and an amorphous pET sheet (Tg: about 75 ° C) were formed by a T-die extrusion method. The amorphous PET sheet is fed to the sheet-making device 1 2, and a prism having a plurality of prisms of 4 waist triangles which are arranged in the array shape I- TI ^ 顶 on the sheet surface at the apex angle 90 is produced under the following conditions. sheet. [Production conditions] 126535.doc -30- 200900224 Sheet material: amorphous PET thickness. 10 0 μηι Prismatic pitch: 1 〇〇 μιη Surface temperature of the heating roller 11: 15 〇. Surface temperature of the rolling roll 15: 50°c Surface temperature of the cooling roll 12: 30° C Surface temperature of the opposing roller 16: 30 〇 C Cooling speed of the resin sheet: 6 ° C / sec (sheet feeding speed: 2 m / Min) The nip line pressure between the heating roller 11 and the roller 15: 20 kg/cm (Example 13) An amorphous PEN sheet having a thickness of 300 μm was formed by a die-die extrusion method (Tg: about 120° 〇. The amorphous PEN sheet was fed to the sheet manufacturing apparatus 1 or 2, and a prism sheet having a plurality of prisms of an isosceles triangle arranged in an array on the surface of the sheet at an apex angle 90 was fabricated under the following conditions. [Manufacturing conditions] Material: Amorphous pen Thickness: 300 μη Prism spacing: 50 μηι Surface temperature of the heating roller 11: 190 ° C Surface temperature of the roller 15: 8 Surface temperature of the cooling roller 12: 6 (surface temperature of the TC opposing roller 16) : 60 ° C Resin sheet cooling rate: 5 ° C / sec 126535.doc • 31 - 200900224 (sheet feed speed: 3 m / min) Rolling line pressure between the heating roller 11 and the roll 15: 20 kg / cm (Comparative Example 1) An amorphous PET sheet having a thickness of 200 μm (Tg: about 75 ° C) was formed by a T-die extrusion method. The sheet was fed to the sheet manufacturing apparatus 1 or 2, and a prism sheet having a plurality of prisms of an isosceles triangle arranged in an array on the sheet surface at the apex angle 90 was fabricated under the following conditions. [Production conditions] Sheet material: amorphous PET thickness: 200 μηη Prism spacing: 100 μηη Surface temperature of the heating roller 11: 170°C Surface temperature of the roller 15: 4°°C Surface temperature of the cooling roller 12: 30°C Surface temperature of the opposing roller 16: 3 (Cooling speed of TC resin sheet: 3t: /sec I' (sheet feeding speed: 4 m/min) Rolling line pressure between heating roller 11 and roller 15: 15 kg/em (Comparative Example 2) An amorphous pEN sheet having a thickness of 200 μm was formed by a τ-die extrusion method (Tg: about 12 Å. 非晶. The amorphous pEN sheet was fed to the sheet manufacturing apparatus 1 or 2, and manufactured under the following conditions with many arrays Formed on the surface of the sheet with a vertex angle of 90. The prismatic piece of the prism of the isosceles triangle. [Manufacturing conditions] 126535.doc • 32- 200900224
片材料:非晶形PEN 厚度· 200 pm 稜柱間距:1〇〇 μιη 加熱輥11之表面溫度:l70°c 軋輥15之表面温度:60°C 冷卻輥12之表面溫度:30°C 對置輥16之表面溫度:30°C 樹脂片之冷卻速度:20°C/sec (片饋送速度:5 m/min) 加熱輥11與軋輥15之間的軋點線壓力:15 kg/cm (比較實例3) 藉由T形模具擠出法形成5 60 μπι厚度之非晶形pen片 (Tg:約12〇。〇。將非晶形pEN片饋送至片製造裝置丄或^ 且在以下條件下製造具有許多個以陣列形式排 上頂角90。之等腰三角形之稜柱的稜柱片。 、 [製造條件] 片材料:非晶形PEN 厚度:560 μιη 稜枉間距:200 加熱輥11之表面溫度:190°C 軋親1 5之表面溫度:8 0 °C 冷卻親12之表面溫度:3(TC 對置輥16之表面溫度:30°C 樹脂片之冷卻速度:3 °C /sec 126535.doc •33- 200900224 (片饋送速度:2 m/min) 加熱輥11與軋輥15之間的軋點線壓力:15kg/cm (比較實例4) 藉由T形模具擠出法形成200 μπι厚度之非晶形PET片 (Tg :約75°〇。將非晶形PET片饋送至片製造裝置1或2, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90。之等腰三角形之棱柱的稜柱片。 [製造條件]Sheet material: amorphous PEN thickness · 200 pm prism spacing: 1 〇〇 μηη Surface temperature of the heating roller 11: l70 °c Surface temperature of the roller 15: 60 ° C Surface temperature of the cooling roller 12: 30 ° C Opposite roller 16 Surface temperature: 30 ° C Cooling speed of resin sheet: 20 ° C / sec (sheet feeding speed: 5 m / min) Rolling line pressure between heating roller 11 and roll 15 : 15 kg / cm (Comparative Example 3 An amorphous pen sheet having a thickness of 5 60 μm was formed by a T-die extrusion method (Tg: about 12 Å. 非晶. The amorphous pEN sheet was fed to a sheet manufacturing apparatus ^ or ^ and manufactured under the following conditions. The prism sheet of the apex angle of the isosceles triangle is arranged in the form of an array. [Production conditions] Sheet material: Amorphous PEN Thickness: 560 μηη Pitch spacing: 200 Surface temperature of the heating roller 11: 190 ° C Surface temperature of pro 1 5 : 80 ° C Surface temperature of cooling pro 12 : 3 (surface temperature of TC opposing roller 16 : 30 ° C Cooling speed of resin sheet: 3 ° C / sec 126535.doc • 33- 200900224 (Sheet feeding speed: 2 m/min) The nip line pressure between the heating roller 11 and the roll 15: 15 kg/cm (Comparative Example 4) A T-die extrusion method forms an amorphous PET sheet having a thickness of 200 μm (Tg: about 75° 〇. The amorphous PET sheet is fed to the sheet manufacturing apparatus 1 or 2, and is manufactured in a number of arrays under the following conditions. On the surface of the sheet, the apex angle of 90. The prismatic piece of the prism of the isosceles triangle. [Manufacturing conditions]
〔 片材料:非晶形PET 厚度:200 μιη 稜柱間距:50 μηι 加熱輥11之表面溫度:150°C 軋輥15之表面溫度:40°C 冷卻輥12之表面溫度:30°C 對置輥16之表面溫度:30°C 樹脂片之冷卻速度:1〇 °C/ sec ι (片饋送速度:4 m/min) 加熱輥11與軋輥15之間的軋點線壓力:3 kg/em (比較實例5) 藉由T形模具擠出法形成200 μΐη厚度之非晶形ρΕτ片 (Tg.約75C)。將非晶形PET片饋送至片製造裝置1戈2 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90。之等腰三角形之稜柱的稜柱片。 [製造條件] 126535.doc •34- 200900224[Sheet material: amorphous PET thickness: 200 μη Prism spacing: 50 μηι Surface temperature of heating roller 11: 150 ° C Surface temperature of roll 15: 40 ° C Surface temperature of cooling roll 12: 30 ° C Counter roller 16 Surface temperature: 30 ° C Cooling speed of resin sheet: 1 ° C / sec ι (sheet feeding speed: 4 m / min) Rolling line pressure between heating roller 11 and roll 15 : 3 kg / em (Comparative example 5) An amorphous ρΕτ sheet (Tg. about 75 C) having a thickness of 200 μΐ is formed by a T-die extrusion method. The amorphous PET sheet was fed to the sheet manufacturing apparatus 1 and manufactured under the following conditions to have a plurality of apex angles 90 arranged in an array on the sheet surface. The prismatic piece of the prism of the isosceles triangle. [Production conditions] 126535.doc •34- 200900224
片材料:非晶形PET 厚度.200 μπι 稜柱間距:50 μιηSheet material: amorphous PET thickness. 200 μπι Prismatic spacing: 50 μιη
加熱輥11之表面溫度:150°CSurface temperature of heating roller 11: 150 ° C
軋輥15之表面溫度:4(TCSurface temperature of roll 15: 4 (TC
冷卻輥12之表面溫度:30°C 對置輥16之表面溫度:30T: 樹脂片之冷卻速度:l〇°C/sec (片饋送速度:4m/min) 加熱輥11與軋輥15之間的軋點線壓力:35 kg/cm (比較實例6) 藉由T形模具擠出法形成200 μιη厚度之非晶形pET片 (Tg :約75°〇。將非晶形PET片饋送至片製造裝置】或2, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90之專腰二角形之棱柱的棱柱片。 [製造條件] 片材料:非晶形PET 厚度:200 μιη 棱柱間距:50 μηι 加熱輥11之表面溫度:15 0 °C 軋輥15之表面溫度·· 40°C 冷卻輥12之表面溫度:80°C 對置輥16之表面溫度:80°C 樹脂片之冷卻速度:10°C/sec 126535.doc -35 - 200900224 (片饋送速度:3 m/min) 加熱輥11與軋輥15之間的軋點線壓力:15 kg/cm (比較實例7) 藉由T形模具擠出法形成1〇〇 厚度之非晶形片 (Tg :約75°〇。將非晶形PET片饋送至片製造裝置】或2, 且在以下條件下製造具有許多個以陣列形式排列於片表面 上頂角90。之等腰三角形之稜柱的稜柱片。 [製造條件] 片材料:非晶形PET 厚度:100 μηι 棱柱間距:1 85 μιη 加熱輥11之表面溫度·· 15〇°C 軋輥15之表面溫度:4〇°C 冷卻輥12之表面溫度:50°C 對置輥16之表面溫度:5〇°c 樹脂片之冷卻速度:l〇°C/sec (片饋送速度:3 m/min) 加熱輥11與軋輥15之間的軋點線壓力:l5kg/em (比較實例8) 藉由T形模具擠出法形成200 μηι厚度之非晶形叩丁片 (Tg :約75。〇。在以下條件下,將非晶形ρΕτ片用於藉由 熔體擠出法製造具有許多個以陣列形式排列於片表面上頂 角90。之等腰三角形之稜柱的稜柱片。 [製造條件] 126535.doc • 36- 200900224 片材料:非晶形PET 厚度:200 μιη 稜柱間距:5 0 μηι 圖集體展示第1至第13實例及第1至第8比較實例之片 製造條件。 接下來’分別量測在第1至第丨3實例及第1至第8比較實 例之製造條件下所製造之樣本的稜柱形狀轉印率(%)、稜 柱棱角之曲率半徑(頂角κ(μιη))、稜柱高度與片之總厚度 之稜柱比率(%)、結晶率(%)及正面亮度提高率…卜 先前已描述轉印率之定義。藉由差示掃描量熱計 (jhfferentlai scanning ,dsc)經由密度計算來 里測、、σ日日率。正面焭度提高率為當在以下條件下提供該等 實例及比較實例中之每一者之棱柱片樣本及漫射片時正面 亮度之提高率:模型為圖5中所示之液晶顯示袭置之組 態,且既不具有稜柱片10亦不具有漫射片23之在暗室中之 ^面亮度將為標準值(_)4面亮度係藉由由κ〇心 Μ:1™1一.所製造之儀器^ 畺測結果展示於圖11令。你一 ^ .,. 吏用二級評判(three-grade judgmg),且評估標準包括: 更為優良的水準H 與“產物相比實際上 ^不在實際上無問題的水準之 及U在實際上不合格特性水準之"X”。 如圖η中所示,第i至第 或更高之轉印率。❹❹< ^之:一樣本均具有· 或更小,從而證明了極佳轉印…徑為稜柱間距之5% 轉印精度。另外,每-樣本均具 126535.doc -37- 200900224 有1 〇%或更小之文抑制結晶率,且未觀測到由變白所引起 之透明度降低。關於每一樣本,液晶顯示裝置之正面亮度 改良了 180%或更高。 雖然第1個比較實例具有高轉印率,但是因為結晶率超 過20%且透明度因變白而降低,故正面亮度之提高率保持 在175%。此可歸因於加熱輥!〗之表面溫度較高(超過 Tg+90°C )及不可獲得防止結晶所必需之冷卻速度的因素。 雖然第2比較實例能夠防止結晶之進行,但是轉印率較低 且π度之提冋亦不足。此可歸因於加熱輥u之表面溫度較 低(低於Tg+60°C)、形態轉印不足之因素。比較實例3之樹 脂片過厚達560 μιη,因此冷卻速度不足,結晶過度進行且 透射率因變白而降低。 因為加熱輥11與軋輥15之間的軋點線壓力過低達3 kg/cm,故第4比較實例具有不足之形態轉印且不能獲得正 面亮度的高提高率。另一方面,關於第5比較實例,因為 軋點線壓力過高達35 kg/cm,故穩定之片製造為不可能 的。另外,關於第6比較實例,因為冷卻輥12之表面溫度 較高(超過Tg)且脫離效能較差,故片之穩定製造為不可能 的。 第7比較實例具有棱柱高度與總片厚度之高(超過比 率’因此片沿著稜柱隆脊方向撕裂,引起裂痕或其類似物 而具有不良耐久性及處理,且穩定生產為不可能的。因為 第8比較實例之形態轉印使用了熔體擠出&,故轉印率較 差且未觀測到亮度之極佳提高。 126535.doc -38- 200900224 在冷卻速度不慢於5 °C/ sec且不快於40 °C/ see之第1至第i3 實例中,加熱輥11之表面溫度不低於Tg+6〇t:且不高於 Tg+90 C且樹脂片之厚度為500 μπι或更薄,有可能防止片 之過度結晶且結晶率可被抑制於20%或更小。因為軋點線 壓力滿足不低於5 kg/cm且不高於30 kg/cm之條件,故可獲 得極佳形態轉印效能及脫離效能以實現穩定生產率。 雖然已描述本發明之實施例及實例’但是顯然本發明並 不限於彼等,且基於本發明之技術概念,各種修改為可能 的。 舉例而言’在該等實施例中,將在卷狀態下之樹脂片J 〇 或被切割成片尺寸(sheet size)之樹脂片饋送至片製造裝置 1及2。替代地,可將用於製造非晶態樹脂片之熔體擠出裝 置女裝於片製造裝置之前端平台側以連續執行樹脂片製造 及軋花。 可將用於在預定方向上拉伸所製造之軋花片之拉伸裝置 安裝於片製造裝置之後端平台側以連續執行軋花加工及拉 伸處理。 熟習此項技術者應理解,各種修改、組合、次組合及變 更可在其係屬於隨时請專利範圍或其等效物之範嘴内的 限度内視設計需求及其他因素而產生。 本發明文獻含有與於2007年3月16日在曰本專利局申請 之曰本專利申請案第20〇7_〇69639號及於2〇〇8年丨月Μ曰在 日本專利局中請之日本專利巾請案第__號相關 的標的物,該等申請案之全部内容係以引用的方式併入本 126535.doc -39· 200900224 文中。 【圖式簡單說明】 圖1為展示用於根據本發明之-第-實施例之光學片製 造方法之片製造裝置的輪廓結構的圖式; 圖2A及2B為展示^中所示之片製造裝置之樹腊片之乾 花帶及軋花形成平面的主要部分的放大橫截面圖; 圖3為解釋藉由㈣方法之圖案轉印與藉由溶體擠出法 之圖案轉印之間的圖案轉印效能差異的實驗結果的曲線 圖; 圖4為展示藉由圖1中所示之片製造裝置所製造之樹脂片 (光學片)之總體結構的透視圖; 圖5為展示使用圖4中所示之光學片作為稜柱片之液晶 示裝置之輪廓結構的圖式; 曰 圖6為展示用於根據本發明之—第二實施例之光學片製 造方法之片製造裝置的輪廓結構的圖式; 圖7為解釋根據本發明之一第三實施例之光學片製造 法的圖式; 圖8A及8B為展示加熱輥及冷卻輥之溫度分布的圖式. 實例的圖式; 圖9A至9E為展示形成於樹脂片之表面上之軋花形狀之 圖10為展示本發明中之實例之結果的表;及 圖11為展示本發明中之實例之結果的表。 【主要元件符號說明】 1 片製造裝置 126535.doc -40- 200900224 2 片製造裝置 10 樹脂片/棱柱片 10a 軋花形狀/稜柱圖案 10L 層壓片 10s 樹脂片 lOt 樹脂片 11 加熱報 12 冷卻輥 13 軋花帶 13a 軋花形狀/幾何形狀設計 14 金屬環形帶 15 軋輥 16 對置輥/背托輥 20 液晶顯不裝置 21 液晶顯不面板 22A 第一偏光器 22B 第二偏光器 23 漫射片 24 背光單元 a 軸線 b 轴線 HI 形成於軋花帶13上之軋花形狀高度 H2 形成於樹脂片10上之軋花形狀高度 126535.doc -41 -Surface temperature of the cooling roll 12: 30 ° C Surface temperature of the opposing roller 16: 30T: Cooling speed of the resin sheet: 10 ° C / sec (sheet feeding speed: 4 m / min) Between the heating roller 11 and the roller 15 Rolling line pressure: 35 kg/cm (Comparative Example 6) An amorphous pET sheet having a thickness of 200 μm was formed by a T-die extrusion method (Tg: about 75° 〇. Amorphous PET sheet was fed to a sheet manufacturing apparatus) Or 2, and under the following conditions, a prism sheet having a plurality of prismatic prisms arranged in an array on the top surface of the sheet surface at the apex angle 90. [Production conditions] Sheet material: amorphous PET Thickness: 200 μm Prism pitch : 50 μηι Surface temperature of the heating roller 11: 15 0 °C Surface temperature of the roller 15 · 40 ° C Surface temperature of the cooling roller 12: 80 ° C Surface temperature of the opposing roller 16: 80 ° C Cooling speed of the resin sheet : 10 ° C / sec 126535.doc - 35 - 200900224 (sheet feeding speed: 3 m / min) nip line pressure between the heating roller 11 and the roll 15: 15 kg / cm (Comparative Example 7) by T-shaped The die extrusion method forms an amorphous sheet having a thickness of 1 ( (Tg: about 75° 〇. feeding the amorphous PET sheet to the sheet manufacturing apparatus) or 2, And a prism sheet having a plurality of prisms of an isosceles triangle arranged in an array on the surface of the sheet at an apex angle of 90. [Production conditions] Sheet material: amorphous PET Thickness: 100 μηι Prismatic pitch: 1 85 Μιη Surface temperature of the heating roller 11··15〇°C Surface temperature of the roll 15: 4〇°C Surface temperature of the cooling roll 12: 50°C Surface temperature of the opposing roller 16: 5〇°c Cooling speed of the resin sheet : l 〇 ° C / sec (sheet feeding speed: 3 m / min) nip line pressure between the heating roller 11 and the roller 15: l5 kg / em (Comparative Example 8) 200 μm by T-die extrusion method Amorphous butadiene sheet having a thickness (Tg: about 75 Å. The amorphous ρ Ε τ sheet is used for the production by the melt extrusion method to have a plurality of apex angles 90 arranged in an array on the sheet surface under the following conditions. Prismatic piece of the isosceles triangle prism. [Manufacturing conditions] 126535.doc • 36- 200900224 Sheet material: Amorphous PET Thickness: 200 μιη Prism spacing: 5 0 μηι Figure collectively shows the first to the thirteenth and the first to The sheet manufacturing conditions of the eighth comparative example. Next, 'measured separately The prism shape transfer rate (%) of the sample manufactured under the manufacturing conditions of the first to third examples and the first to eighth comparative examples, the radius of curvature of the prism corner (the apex angle κ (μιη)), the prism height and The prism ratio (%), the crystallization ratio (%), and the front luminance increase rate of the total thickness of the sheet... The definition of the transfer rate has been previously described. The σ day rate is measured by density calculation by a differential scanning calorimeter (dsc). The positive enthalpy increase rate is the rate of increase in frontal brightness when the prismatic sheet sample and the diffusing sheet of each of the examples and comparative examples are provided under the following conditions: the model is the liquid crystal display as shown in FIG. The configuration, and neither the prismatic sheet nor the diffusing sheet 23 in the darkroom will have a standard value (_) 4 plane brightness by κ〇 heart: 1TM1. The manufactured instrument ^ test results are shown in Figure 11. You are using a three-grade judgmg, and the evaluation criteria include: A better level H is actually compared to the product. Actually, it is not actually a problem-free level and U is actually Unqualified characteristic level "X". The transfer rate of the ith to the first or higher as shown in Fig. η. ❹❹<^之: The same as this has or is smaller, which proves that the excellent transfer... diameter is 5% of the prism pitch. In addition, each sample had 126535.doc -37-200900224 with a reduction of crystallization rate of 1% or less, and no decrease in transparency caused by whitening was observed. With respect to each sample, the front luminance of the liquid crystal display device was improved by 180% or more. Although the first comparative example has a high transfer rate, since the crystallization ratio exceeds 20% and the transparency is lowered by whitening, the increase rate of the front luminance is maintained at 175%. This can be attributed to the heating roller! The surface temperature is higher (over Tg + 90 ° C) and the cooling rate necessary to prevent crystallization is not available. Although the second comparative example can prevent the progress of crystallization, the transfer rate is low and the π degree is insufficient. This is attributable to the fact that the surface temperature of the heating roller u is low (less than Tg + 60 ° C) and the form transfer is insufficient. The resin sheet of Comparative Example 3 was too thick to be 560 μm, so that the cooling rate was insufficient, the crystallization was excessively performed, and the transmittance was lowered due to whitening. Since the nip line pressure between the heating roller 11 and the roll 15 was as low as 3 kg/cm, the fourth comparative example had insufficient form transfer and a high rate of improvement in front surface luminance could not be obtained. On the other hand, regarding the fifth comparative example, since the nip line pressure was as high as 35 kg/cm, stable sheet production was impossible. Further, regarding the sixth comparative example, since the surface temperature of the cooling roll 12 is high (over Tg) and the detachment efficiency is poor, stable production of the sheet is impossible. The seventh comparative example has a high prism height and a total sheet thickness (exceeding the ratio 'so the sheet is torn in the direction of the prism ridge, causing cracks or the like to have poor durability and handling, and stable production is impossible. Since the morphology transfer of the eighth comparative example uses melt extrusion &, the transfer rate is poor and no excellent increase in brightness is observed. 126535.doc -38- 200900224 The cooling rate is not slower than 5 °C/ In the first to the i3th examples of sec and not faster than 40 ° C / see, the surface temperature of the heating roller 11 is not lower than Tg + 6 〇 t: and not higher than Tg + 90 C and the thickness of the resin sheet is 500 μπι or Thinner, it is possible to prevent excessive crystallization of the sheet and the crystallization rate can be suppressed to 20% or less. Since the nip line pressure satisfies the conditions of not less than 5 kg/cm and not more than 30 kg/cm, it is available. Excellent morphological transfer performance and detachment performance to achieve stable productivity. Although the embodiments and examples of the present invention have been described, it is apparent that the present invention is not limited to them, and various modifications are possible based on the technical concept of the present invention. In terms of 'in these embodiments, will be in the volume A resin sheet J 〇 or a resin sheet cut into a sheet size is fed to the sheet manufacturing apparatuses 1 and 2. Alternatively, a melt extrusion apparatus for manufacturing an amorphous resin sheet may be used. The resin sheet is continuously produced and embossed on the front platform side of the sheet manufacturing apparatus. The stretching apparatus for stretching the manufactured embossed sheet in a predetermined direction can be attached to the rear end side of the sheet manufacturing apparatus to be continuously executed. The embossing process and the stretching process. It should be understood by those skilled in the art that various modifications, combinations, sub-combinations and alterations may be considered within the limits of the scope of the patent application or its equivalent. And other factors. The document of the present invention contains the patent application No. 20〇7_〇69639, which was filed on March 16, 2007 at the Patent Office of the present invention, and Japanese Patent Office, please refer to the subject matter of the Japanese Patent Towel No. __, the entire contents of which are incorporated by reference in the text of 126535.doc -39· 200900224. [Simple description] Figure 1 is a representation for use in accordance with the present invention - Figure 2A and 2B show the main structure of the dried flower ribbon and the embossing plane of the slab of the sheet manufacturing apparatus shown in Fig. 2; Partial enlarged cross-sectional view; Fig. 3 is a graph explaining experimental results of pattern transfer efficiency difference between pattern transfer by the (4) method and pattern transfer by solution extrusion method; A perspective view of the overall structure of a resin sheet (optical sheet) manufactured by the sheet manufacturing apparatus shown in Fig. 1; Fig. 5 is a view showing a contour structure of a liquid crystal display apparatus using the optical sheet shown in Fig. 4 as a prism sheet FIG. 6 is a view showing a outline structure of a sheet manufacturing apparatus for an optical sheet manufacturing method according to a second embodiment of the present invention; FIG. 7 is a view explaining a third embodiment of the present invention. Fig. 8A and Fig. 8B are diagrams showing the temperature distribution of the heating roller and the cooling roller. Fig. 9A to Fig. 9E are diagrams showing the shape of the embossing formed on the surface of the resin sheet. 10 is a diagram showing an example of the present invention Table of the results; and Figure 11 is a table showing the results of the examples in the present invention. [Description of main component symbols] 1 sheet manufacturing apparatus 126535.doc -40- 200900224 2 Sheet manufacturing apparatus 10 Resin sheet/prism sheet 10a embossed shape/prism pattern 10L Laminate 10s Resin sheet lOt Resin sheet 11 Heated report 12 Cooling roll 13 embossed belt 13a embossed shape / geometry design 14 metal endless belt 15 roll 16 opposite roller / backing roller 20 liquid crystal display device 21 liquid crystal display panel 22A first polarizer 22B second polarizer 23 diffuser 24 backlight unit a axis b axis HI embossed shape height H2 formed on embossed belt 13 embossed shape height formed on resin sheet 10 126535.doc -41 -
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Also Published As
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CN101308222B (en) | 2011-07-20 |
JP5152528B2 (en) | 2013-02-27 |
JP2010058521A (en) | 2010-03-18 |
CN101308222A (en) | 2008-11-19 |
KR101708926B1 (en) | 2017-02-21 |
JP2008260268A (en) | 2008-10-30 |
TWI388419B (en) | 2013-03-11 |
JP4450078B2 (en) | 2010-04-14 |
KR20080084690A (en) | 2008-09-19 |
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