TW201132686A - Solution casting method - Google Patents
Solution casting method Download PDFInfo
- Publication number
- TW201132686A TW201132686A TW100108765A TW100108765A TW201132686A TW 201132686 A TW201132686 A TW 201132686A TW 100108765 A TW100108765 A TW 100108765A TW 100108765 A TW100108765 A TW 100108765A TW 201132686 A TW201132686 A TW 201132686A
- Authority
- TW
- Taiwan
- Prior art keywords
- film
- space
- peeling
- wet
- wet film
- Prior art date
Links
- 238000005266 casting Methods 0.000 title claims abstract description 31
- 238000000034 method Methods 0.000 title claims description 42
- 239000002904 solvent Substances 0.000 claims description 14
- 238000011144 upstream manufacturing Methods 0.000 claims description 11
- 229920000642 polymer Polymers 0.000 claims description 6
- 238000001035 drying Methods 0.000 description 16
- 238000001816 cooling Methods 0.000 description 12
- 238000001879 gelation Methods 0.000 description 11
- 239000000243 solution Substances 0.000 description 11
- 238000009736 wetting Methods 0.000 description 8
- 238000004804 winding Methods 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 6
- 230000001681 protective effect Effects 0.000 description 6
- 239000000758 substrate Substances 0.000 description 6
- 239000011521 glass Substances 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 239000000853 adhesive Substances 0.000 description 3
- 230000001070 adhesive effect Effects 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000003287 optical effect Effects 0.000 description 3
- 229920006254 polymer film Polymers 0.000 description 3
- 150000001412 amines Chemical class 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 230000006837 decompression Effects 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 230000035922 thirst Effects 0.000 description 2
- 241001674044 Blattodea Species 0.000 description 1
- 241000283690 Bos taurus Species 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 1
- VCUFZILGIRCDQQ-KRWDZBQOSA-N N-[[(5S)-2-oxo-3-(2-oxo-3H-1,3-benzoxazol-6-yl)-1,3-oxazolidin-5-yl]methyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C1O[C@H](CN1C1=CC2=C(NC(O2)=O)C=C1)CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F VCUFZILGIRCDQQ-KRWDZBQOSA-N 0.000 description 1
- 206010036790 Productive cough Diseases 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- 229910000416 bismuth oxide Inorganic materials 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 230000009194 climbing Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 108010058391 cyclic(RGDfK)16 peptide Proteins 0.000 description 1
- 210000003298 dental enamel Anatomy 0.000 description 1
- TYIXMATWDRGMPF-UHFFFAOYSA-N dibismuth;oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Bi+3].[Bi+3] TYIXMATWDRGMPF-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000012840 feeding operation Methods 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 230000005923 long-lasting effect Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 210000003802 sputum Anatomy 0.000 description 1
- 208000024794 sputum Diseases 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 230000000153 supplemental effect Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
- B29C41/24—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of indefinite length
- B29C41/26—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of indefinite length by depositing flowable material on a rotating drum
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
- B29C41/34—Component parts, details or accessories; Auxiliary operations
- B29C41/42—Removing articles from moulds, cores or other substrates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
- B29C41/34—Component parts, details or accessories; Auxiliary operations
- B29C41/52—Measuring, controlling or regulating
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Moulding By Coating Moulds (AREA)
- Polarising Elements (AREA)
Abstract
Description
201132686 i//5Zpit 六、發明說明: 【發明所屬之技術領域】 於一種製造聚合物膜之溶液製膜方法。 【先前技術】 、纖維素醯化物職環狀_烴_各娜合物膜以依 =途t尺利用。切割有時在與應該組合的構件組 行,但也有時在與應該組合的構 貼請…、構件—同進行。例如,在製造偏光板時, 作保護該偏光膜之保護膜的聚合物膜之 ‘胺由理。另外’將配設在偏光膜兩面的-對保 二乂其:―方代替成光學補償膜(包含相位差膜)時 也相,。這樣也有時將光學補伽作為保護膜使用。201132686 i//5Zpit VI. Description of the Invention: [Technical Field of the Invention] A method for forming a solution for producing a polymer film. [Prior Art], cellulose bismuth oxide ring-hydrocarbon _ each film is used according to the way. Cutting is sometimes done in groups that should be combined, but sometimes in the same way as the combination that should be combined. For example, in the production of a polarizing plate, the amine film of the protective film which protects the polarizing film is made of an amine. In addition, when the two sides of the polarizing film are disposed on the opposite side of the polarizing film, the side is replaced by an optical compensation film (including a retardation film). In this way, optical supplemental gamma is sometimes used as a protective film.
Am了由包括偏細與保護敎貼合的多層構造之膜做 成偏光板而切割成預期尺寸時,從其中一方的膜面按壓切 j刀料對多層構造朗行_。像域 f’則有時從由切割形成的切割面向保護膜内』生裂 ί。因切割而產生這種裂紋的保_被評價為加工適性 差,所得到的偏光板的商品價值也明顯變低。 並^在製造液晶顯示器時,將偏光板貼附在玻璃基 :=璃基板剝下偏光板之後再貼合這樣 有時保護膜之—部份殘留== 基板上。這樣不會剝下整體而一部份殘留在破螭基板上這 201132686 37782pif 樣的保護膜被評價為返工性差,故而非較佳方式。 人為製造如上前述在顯示裝置等光學用途巾使用的聚 S,膜之方法,有騎製财法。轉伽方法係將在溶 射洛解了聚合物之濃液在支#體上流延而形成流延膜, 凝固該流賴而_ ’將_的流賴 物膜之製細。該溶液製膜根據流= <所周知有乾燥流延方式和冷卻凝膠化流延方式。 乾燥流延方式係將流延膜乾燥至預期的乾燥水平,藉 凝固流延膜者。亦即,剝離後乾燥流延膜直到濕 '、成為可傳送狀態這樣的程度而進行凝固。 目對’冷卻凝膠化流延方式係藉由冷卻流延膜在 =殘留率非常高的狀態下做成凝膠狀,並凝固成即使剝 也可以傳送之程度為止進行凝膠化。 ^較上述乾燥流延方式與冷卻凝膠化流延方式,後者 夠在溶劑殘留率高時從支撐體剝下來故而在製造 這一點上明顯處於優勢。但是,用冷卻凝膠化流延方 χ侍到的聚合物膜在上述的加工適性和 不如用乾燥流延方式制㈣合物^丨之觀』上 樣,為/顯現所需性能的同時,像冷卻凝膠化流延方式那 至入有效地製造,亦即,提高每單位時間内的膜的製造量, 號二提出了各種提案。例如,在日本專利公開2000-239403 位ί報法中,提出了在從支撐體上剝下流延膜之剝離 噴吹氣流的方法。根據此方法,能夠有效地製造出具 有預期延遲之膜。 6 201132686 37782pif 另外’日本專利公開2001-198933號公報中,從喷嘴 向剛剝離後的濕潤膜的從支撐體剝離之膜面以相對於膜面 成垂直方向之方式喷吹風速為20m/秒以上之風。日本專利 公開2001-198933號公報中,由此,即使從支撐體剝離時 的溶劑殘留率為100%以上的高值時,亦可從支撐體穩定 地剝離流延膜而製造出平面性優異之聚合物膜。 但是’即使將日本專利公開2000-239403號公報、日 本專利公開2001-198933號公報之方法適用於以高溶劑殘 留率剝離而乾燥之冷卻凝膠化流延方式中,也無法兼顧加 工適性及返工性之改善。 【發明内容】 因此,本發明的目的在於提供一種提高用冷卻凝膠化 流延方式制作之膜的加工適性和返工性之溶液製膜方法。 本發明之溶液製膜方法具備流延膜形成步驟、流延膜 冷卻步驟、剝離步驟、壓力控制步驟及乾燥步驟。流延膜 形成步驟中,藉由將溶劑中溶解了聚合物之濃液連續流延 在支撐體上而形成流延膜。流延膜冷卻步驟中,將前述流 延膜冷卻並凝固。剝離步驟中:剝離前述流延膜而得到濕 潤膜。在殘留有前述溶劑的狀態下剝離前述流延膜。藉由 將前述濕潤膜捲繞在觀的周面並傳送前述濕潤膜來剝離前 述流延膜。前述輥配设成其長邊方向與前述支撐體之流延 面的寬度方向一致。刖述輥具備於前述濕潤膜之傳送路上 與前述支撐體相反的一側。壓力控制步驟中,使比前述輥 更罪近上游之刖述第2空間之麼力小於前述第1空間之壓Am, when a polarizing plate is formed by a film having a multilayer structure including a thinned and protective enamel, and is cut into a desired size, pressing the cutting blade from one of the film faces is performed on the multilayer structure. The image field f' sometimes cracks from the cut formed by the cut surface toward the protective film. The protection of such cracks due to the cutting was evaluated as poor workability, and the commercial value of the obtained polarizing plate was also remarkably low. And in the manufacture of the liquid crystal display, the polarizing plate is attached to the glass base: = the glass substrate is peeled off after the polarizing plate is attached, and sometimes the protective film is partially residual == on the substrate. This does not peel off the whole part and remains on the broken substrate. This 201132686 37782pif-like protective film is evaluated as poor reworkability, and is not preferred. The method of artificially producing the poly S film used in the optical use towel such as a display device as described above is a riding method. The transfer gamma method is to form a cast film by laminating the concentrated solution of the polymer on the support to form a cast film, and solidifying the flow to form a flow film of the flow. The film formation of this solution is known as a dry casting method and a cooling gelation casting method according to the flow rate. The dry casting method is to dry the cast film to the desired level of drying by solidifying the cast film. In other words, after the peeling, the cast film is dried until it is wet and is in a transportable state. The cooling gelation casting method is formed into a gel state by a cooling cast film in a state where the residual ratio is extremely high, and is solidified to gelation even if peeling can be carried out. Compared with the above dry casting method and the cooling gelation casting method, the latter can be peeled off from the support when the solvent residual rate is high, so that it is obviously advantageous in manufacturing. However, the polymer film which is cooled by the gelation casting is loaded in the above-mentioned processing suitability and is not as good as the dry casting method, and the desired performance is exhibited/imaged. The cooling gelation casting method is effective to manufacture, that is, to increase the amount of film produced per unit time, and various proposals have been made. For example, in Japanese Patent Laid-Open No. 2000-239403, a method of peeling off a blown air stream of a cast film from a support is proposed. According to this method, a film having an intended retardation can be efficiently produced. In the Japanese Patent Laid-Open Publication No. 2001-198933, the film surface which is separated from the support from the nozzle to the wet film immediately after peeling is sprayed at a speed of 20 m/sec or more in a direction perpendicular to the film surface. The wind. In the case where the solvent residual ratio at the time of peeling from the support is a high value of 100% or more, the cast film can be stably peeled off from the support to produce a flatness. Polymer film. However, even if the method of the Japanese Patent Laid-Open Publication No. 2000-239403 and the Japanese Patent Publication No. 2001-198933 is applied to a cooling gelation casting method in which the high solvent residual ratio is peeled off and dried, the processing suitability and rework cannot be achieved. Improvement of sex. SUMMARY OF THE INVENTION Accordingly, it is an object of the present invention to provide a solution film forming method for improving the processability and reworkability of a film produced by a cooling gelation casting method. The solution film forming method of the present invention comprises a cast film forming step, a cast film cooling step, a peeling step, a pressure control step, and a drying step. In the cast film forming step, a cast film is formed by continuously casting a dope in which a polymer is dissolved in a solvent onto a support. In the casting film cooling step, the aforementioned casting film is cooled and solidified. In the peeling step, the cast film was peeled off to obtain a wet film. The cast film was peeled off while the solvent was left. The cast film is peeled off by winding the wet film around the circumferential surface and transferring the wet film. The roller is disposed such that its longitudinal direction coincides with the width direction of the casting surface of the support. The above-described roll is provided on the side opposite to the support on the conveying path of the wet film. In the pressure control step, the force of the second space is less than the upstream of the roller, and the force of the second space is smaller than the pressure of the first space.
201132686 3//82piI 力’以使朝向前她的前述濕賴之傳送路向 作 =二:Ϊ第1空間為前述濕潤膜的從前述支撐體剝 夕报J中的膜面上之空間。前述第2空間為另-方 膜。、啦間。乾燥步驟巾,將前述賴膜乾燥而做成 該冷液製膜方法中,較佳為藉由吸引氣體之吸 輥更靠近上游之前述第2空間的氣體,“從 月二ΐ伽轉前職延__位置與前_之間的前 述第2空間進行減壓。 較佳為前述吸引裝置具備將應該減壓的前述第2空間 ^外部空間隔_室,藉由調整前述室内之壓力來控制朝 向前述輥的前述濕潤膜之傳送路徑❶ 較佳為藉由控制前述路徑,使前述剝離位置中前述支 芽體之表面與前述濕潤膜所成的角Θ1設為3G。以上80。以 下的範圍。 根據本發明之溶液製膜方法,儘管是冷卻凝膠化流延 χ,也可製造出加工適性和返工性優異的膜。 兴為讓本發明之上述特徵和優點能更明顯易懂,下文特 牛實施例,並配合所附圖式作詳細說明如下。 【實施方式】 第1圖之溶液製膜設備10具備濕潤膜形成裝置17、 1拉幅機18、第2拉幅機19、輥乾燥裝置22及捲取裝 24。濕潤膜形成裝置17由溶劑12中溶解了聚合物u 之濃液13形成濕潤膜16。第1拉幅機18藉由保持機構(未 8 201132686 3//δ2ριί 圖=)保持已形成的濕潤膜之各侧部並傳送的同時 乾燥直到成為-定的溶綱留率。第2拉闕 = 機構(未圖示)保持濕潤膜16之側部並施加寬度二2 適當張力的同時進-步進行乾燥。減縣置2 ’ 傳送經過第2拉幅機19的濕潤膜16的同時,進逢" 乾燥而做賴23。捲取裝置24將乾㈣膜2取= 狀。另外,溶液製膜設備1G具備在第2拉幅機 燥裝置22之間以及輥乾燥裝置22與捲取裝置^之 傳送路切除濕潤膜16和膜23之各側端部的狹 ^ 圖示),但省略圖示。 〈禾 濕潤膜形成裝置17具備作為支樓體之滾筒29 四具有驅動機構(未圖示),藉由該驅動機構在外周= 1由該旋轉,周面29a成為流延濃液13的無_ 滾请29之上方具備有流出濃液n的流延模Μ。醉 :=31連續向旋轉的滾筒29流出濃液13,濃液曰13 當成流延膜32。另外,有關從模31至滾 =9^濃液13 ’雖然在滚筒29之旋轉方向上的上游設置 :,至’但省略圖示。該減壓室吸引流出的濃液13之上游 側區的氣氛而對前述區進行減壓。 心將Ϊ延膜32凝固至依較48可向第1拉幅機18傳送的 二之後’以含溶劑的狀態從滾筒29剝下來。滾筒Μ罝 有^制周面29a的溫度的溫度控制器34。藉由溫度控制器 工制周面29a之溫度’從而將流賴&冷卻成預期的 201132686 3//S2pit 溫度並藉由該冷卻來凝固。 剝離時,由剝離用的輥(以下,稱為剝離輥)33支撐 濕潤膜16,將流延膜32從滾筒29剝下來的剝離位置PP (參照第2圖)保持成恆定。 在剝離輥33之上游設置有對朝向剝離輥33的濕潤膜 16之路彳里進行控制的路徑控制部36。 對於從滾筒29剝離流延膜32之方法,利用其他附圖 進行後述。 =濕_形成裝置17向第丨拉幅機18的轉送部位具 藉由剝離形成的濕潤獏16由這些輥48傳 送並引導至第1拉幅機18。 吁 第1拉幅機18中,由保持機構(夫 16側端部,並由兮俘掊應播德 不)保持潤膜 持機構Α夕盤相二',、ί機構傳送的同時乾燥濕潤膜b。俘201132686 3//82 piI force' is such that the forward path of the wet front toward the front is made = two: The first space is the space on the film surface of the wet film peeled from the support. The second space is a double-sided film. , room. The drying step towel is obtained by drying the film to form the cold liquid film forming method, preferably by sucking a gas suction roll closer to the gas in the second space upstream, "from the second day of the Sangha transfer to the predecessor The second space between the extension __ position and the front _ is depressurized. Preferably, the suction device includes the second space 外部 external space _ chamber to be depressurized, and is controlled by adjusting the pressure in the chamber. Preferably, the transport path ❶ of the wet film facing the roller is controlled such that the angle Θ1 formed by the surface of the branch bud and the wet film in the peeling position is 3 G. The range is 80 or less. According to the solution film forming method of the present invention, a film excellent in processability and reworkability can be produced in spite of cooling gelation cast enthalpy. The above features and advantages of the present invention are more apparent and easy to understand. The embodiment of the specific cattle is described in detail below with reference to the drawings. [Embodiment] The solution film forming apparatus 10 of Fig. 1 includes a wet film forming apparatus 17, a tenter 18, a second tenter 19, and a roller. Drying device 22 and coiling device 24. The wet film forming apparatus 17 forms the wet film 16 from the dope 13 in which the polymer u is dissolved in the solvent 12. The first tenter 18 is maintained by the holding mechanism (not 8 201132686 3//δ2ριί diagram =) Each side of the wet film is conveyed while being dried until it reaches a predetermined retention rate. The second pull = mechanism (not shown) holds the side of the wet film 16 and applies a width of two 2 to the appropriate tension - The drying step is carried out. The county set 2' is conveyed through the wet film 16 of the second tenter 19, and is subjected to "drying and drying. 23. The winding device 24 takes the dry (four) film 2 into a shape. The film forming apparatus 1G includes a narrow view of the end portions of the second tenter drying device 22 and the transfer paths of the roll drying device 22 and the winding device to cut off the respective sides of the wet film 16 and the film 23, but is omitted. The wetting film forming apparatus 17 includes a drum 29 as a branch body, and has a driving mechanism (not shown). The driving mechanism rotates on the outer circumference = 1, and the circumferential surface 29a becomes a casting dope 13 No _ Rolling 29 has a casting die with a flow of concentrated liquid n. Drunk: = 31 continuous rotating drum 29, the dope 13 is discharged, and the dope 13 is formed as a casting film 32. Further, the slave mold 31 to the roll = 9^ dope 13' is disposed upstream in the rotation direction of the drum 29: The decompression chamber attracts the atmosphere of the upstream side region of the effluent concentrate 13 to decompress the region. The heart solidifies the ruthenium film 32 to the second after the transfer to the first tenter 18 The solvent-containing state is peeled off from the drum 29. The drum has a temperature controller 34 that controls the temperature of the circumferential surface 29a. By the temperature controller, the temperature of the peripheral surface 29a is programmed to cool the flow & 201132686 3//S2pit temperature and solidified by this cooling. At the time of peeling, the wet film 16 is supported by a peeling roller (hereinafter referred to as a peeling roll) 33, and the peeling position PP (see Fig. 2) from which the casting film 32 is peeled off from the roll 29 is kept constant. A path control portion 36 that controls the path of the wet film 16 toward the peeling roller 33 is provided upstream of the peeling roller 33. The method of peeling the cast film 32 from the drum 29 will be described later using other drawings. The wetting unit 17 is conveyed to the transfer portion of the second tenter 18 by the peeling of the wet enthalpy 16 formed by the rollers 48 and guided to the first tenter 18. In the first tenter 18, the holding mechanism (the end of the side of the 16th, and the captive of the cockroach should be broadcasted), the film holding mechanism is maintained, and the film is transported by the mechanism. b. Capture
之側端部_制_ 16。各在濕潤膜W 寬度:rrr的同時,向以 把持濕潤膜I6之側端部的夾子^ 、 u保持機構為 對濕潤膜16之寬度方向料預定的^失子在預定的時機 第h第2拉幅機18、19均作、二 第1、第2拉幅機18、19之各内部分,送路的室形成。 在這些導管(未圖示)中與濕_16之、^導管(未圖示)。 形成有多數個進氣喷嘴(未圖示)和„對置而分別 噴嘴(未圖示 201132686 ^7782ριί 氣體11、自第n嘴之乾燥氣體和吸引來自吸引喷嘴之 度及溶L體·^ϋ18、、19之内部被保持成惶定的濕 久肉邱冰二―、、又藉由通過第〗、第2拉幅機18、丨9之 潤膜^,古订濕潤膜16之乾燥。第1拉幅機18中乾燥濕 與此相對,^2成可播由第2拉幅機19的夾子把持之程度。 經過第2拉幅機19的濕潤膜16由狹 ::::連的保持痕二 pg 方的側部與另一方的側墙邮+ 間的中央部被送至輥乾燥裝置22。 。之 若濕賴16㈣线乾縣置22,則由 =列配設的多數個輥21之周面支樓。這些輕21 = 動輕’藉由該驅動輥之旋轉傳适。 輕乾無裝置22具備流出已乾燥氣體的導管 =,作為將送入乾燥氣體的空間與外部隔開的室形^未圖 乾燥裳置22上形成有排氣口,藉由送出來自導,。輥 體和從排氣口排氣,輥乾燥農置22之内部被保巧氣 濕度及溶劑氣體濃度。藉由通過該親乾燥裝置2 ^的 濕潤膜16被乾燥而成為膜23。 内部, 由輥乾燥裝置22乾燥的膜23藉由狹縫裝置 用切割刀刀連續地切割各侧端部而被去除。其中一木圖示) 端部與另一方的侧端部之間的中央部送至捲ς 方的側 捲取成輥狀。 、24並 11 201132686Side end _ system _ 16. At the same time as the wet film W width: rrr, the clips and the u holding means for holding the side end portion of the wet film I6 are predetermined for the width direction of the wet film 16 at the predetermined timing. The tenters 18 and 19 are formed as inner portions of the first and second tenter machines 18 and 19, and the chamber for the passage is formed. In these catheters (not shown), a catheter (not shown) is used. A plurality of inlet nozzles (not shown) and „opposing nozzles are formed separately (not shown in the figure 201132686^7782ριί gas 11, the drying gas from the nth nozzle, and the degree of attraction from the suction nozzle and the L-body 18) , 19, the interior of the 19 is kept as a long-lasting wet long-term meat Qiu Bing II, and by the passage of the first, second tenter 18, 丨9, the ancient wet film 16 is dried. 1 The tenter 18 is dried and wet, and the 2 is formed so as to be able to be gripped by the clip of the second tenter 19. The wet film 16 passing through the second tenter 19 is kept by a narrow:::: The central portion between the side portion of the mark pg side and the side wall of the other side is sent to the roll drying device 22. If the wet line 16 (four) line is located at the county level 22, the plurality of rolls 21 arranged by the = column The circumferential support. These light 21 = moving light 'transmitted by the rotation of the drive roller. The light-drying device 22 has a conduit for flowing out the dry gas = as a space separating the dry gas from the outside The chamber shape is not formed on the dry skirt 22, and is formed by an exhaust port, which is sent out from the guide, and the roller body is exhausted from the exhaust port, and the inside of the roller drying farm 22 is The humidity of the gas and the concentration of the solvent gas are dried by the wet film 16 of the drying device to form the film 23. Internally, the film 23 dried by the roll drying device 22 is continuously cut by a slitting device with a slitting blade. The side ends are cut and removed. One of the woods is shown in the middle portion between the end portion and the other side end portion, and the side portion which is sent to the winding side is taken up into a roll shape. 24, 11 201132686
J / /8/plI 對於剝離工序,參照第2圖及第3圖進行具體說明。 在第2圖、第3圖中,箭頭Z1表示濕潤膜16之傳送方向, 箭頭Z2表不濕潤膜16之寬度方向。另外,周面29a之寬 度方向與濕潤暝16之寬度方向Z1 一致。第2圖及第3圖 為簡要圖’相對於濕潤膜16之厚度較小地描繪剝離輥33。 在以後的說明中,將濕潤膜16的從滚筒29剝下的其 中一方的膜面側之空間稱為第1空間,另一方的膜面侧之 空間稱為第2空間。濕潤膜16的另一方的膜面是指當為流 延膜36時暴露在外部的膜面。剝離輥33配設成其長邊方 向與滾筒29之周面的寬度方向一致。剝離輥33具備於濕 潤膜16之傳送路上與滾筒29相反的一侧。亦即,由於滾 筒29具備於第1空間,因此剝離輥33具備於第2空間。 剝離輞1 33具備驅動機構70和控制器71。控制器71 控制驅動機構70。藉由該驅動機構70,剝離輥33以預定 的轉速在外周方向上旋轉。若被輸入設定的剝離輥33之旋 轉的速度的訊號’則控制器71控制驅動機構7〇使剝離輕 33以其設定速度旋轉。 剝離輕33由周面支撐被引導過來的濕潤膜16,藉由 旋轉傳送濕潤膜16。在以濕潤膜16捲繞於剝離輥33的方 式,配置滾筒29和剝離輥33,並且規定好剝離輥%之下 游的傳送路。像這樣,在剝離輥33使捲繞濕潤膜16,並 由剝離輥33傳送濕潤膜16,由此從滾筒29剝離流延膜32。 另外,剝離輥33可以未必一定是驅動輥,也可以為藉 由在被傳送的濕潤獏16接觸周面而從動的所謂的從動 12 201132686 J7782pif 粃。隹廷種情況下,仕剌離輥〜〜 構。並且,由剝離輥33支撐濕潤獏 ^ 、 迗機 路徑控制部36具備有在滾筒29與剥 2空間。路徑控制部36控制濕潤膜16以翻-曰、第 路徑控制部36具備室55、泵56及控制器▽專送。 室55具備第i構件61、第2構件62、第 第4構件64及第5構件65。第!構 63、 =與讓16的傳送方向Z1上的上游二= h開。第2構件62將應該減壓的第 /工間 ==構件63及第4構件 二側部側之外部空間隔開。第S 仵65將應该減壓的第2空間與下方的外部 = 且,中以被第i構件〜第4構件61 =。並J / /8/plI The peeling process will be specifically described with reference to Figs. 2 and 3 . In Figs. 2 and 3, an arrow Z1 indicates the conveying direction of the wet film 16, and an arrow Z2 indicates the width direction of the wet film 16. Further, the width direction of the circumferential surface 29a coincides with the width direction Z1 of the wetting enthalpy 16. Figs. 2 and 3 are schematic views showing the peeling roller 33 with a small thickness relative to the thickness of the wet film 16. In the following description, the space on the film surface side of the wet film 16 which is peeled off from the drum 29 is referred to as a first space, and the space on the other film surface side is referred to as a second space. The other film surface of the wet film 16 means a film surface exposed to the outside when it is the casting film 36. The peeling roller 33 is disposed such that its longitudinal direction coincides with the width direction of the circumferential surface of the drum 29. The peeling roller 33 is provided on the side opposite to the roller 29 on the conveying path of the wet film 16. In other words, since the drum 29 is provided in the first space, the peeling roller 33 is provided in the second space. The peeling crucible 1 33 is provided with a drive mechanism 70 and a controller 71. The controller 71 controls the drive mechanism 70. By the drive mechanism 70, the peeling roller 33 is rotated in the outer circumferential direction at a predetermined rotation speed. When the signal of the rotational speed of the set peeling roller 33 is input, the controller 71 controls the drive mechanism 7 to rotate the peeling light 33 at its set speed. The peeling light 33 is supported by the circumferential surface to support the wet film 16, and the wet film 16 is conveyed by rotation. The roller 29 and the peeling roller 33 are disposed in such a manner that the wet film 16 is wound around the peeling roller 33, and the transport path below the peeling roller % is defined. In this manner, the wetting film 16 is wound around the peeling roller 33, and the wet film 16 is conveyed by the peeling roller 33, whereby the casting film 32 is peeled off from the drum 29. Further, the peeling roller 33 may not necessarily be a driving roller, and may be a so-called driven 12 201132686 J7782 pif 从 which is driven by the wet raft 16 being conveyed to contact the circumferential surface. In the case of the 隹 种 species, the official 剌 辊 辊 ~ ~ ~ 。. Further, the wetting 貘 ^ is supported by the peeling roller 33, and the weir path control unit 36 is provided with a space between the drum 29 and the stripping unit. The path control unit 36 controls the wet film 16 to be turned over, and the first path control unit 36 includes the chamber 55, the pump 56, and the controller. The chamber 55 includes an i-th member 61, a second member 62, a fourth member 64, and a fifth member 65. The first! The structure 63, = and the upstream direction of the transfer direction Z1 of the 16 is == h. The second member 62 separates the outer space of the side portion side of the second side portion of the second member portion to be depressurized. In the first step 仵65, the second space to be decompressed and the outer portion below are = and the middle member to the fourth member 61 =. and
=與濕潤膜16對置的第1開口 .從該第! J 引^55外部氣體。板狀的第i〜第5構件61〜 = 〜第4構件6卜64以豎立的姿勢配設。 中幻 〃叫®罘i構件61考慮流延膜32 而配設成與滾筒29的距離在觸师以上25⑻帅以^ 13 201132686 37782pif 範圍。傳送方向Z1 t& 滾筒四的下游端29D更靠近上游^ =游知6歸於比 ^ 構件62考慮濕潤膜16之戽声 而配改成與剝離輥33的距離在 予度 的範圍Μ專送方向Z1上的第 =乂上25GG师以下 比剝離輥33的上游端33Uf 、下游端62D位於 件幻形成有第2 = 置m構 ”内部之氣體從該第2開上:。69魏56連接’室 第3構件63和第4構件64配設 16之側緣16e更靠近外側。由此 攀 潤膜16不會與第3構件63及第4磐^^止期間的渴 察時,與濕潤膜16對置的對 ^ ^側方觀 示般’成為不岭、髓〗“丰貫〜方式中第2圖所 以未必一定是曲面之預期路徑重疊的曲面,但也可 之内^Hi内部藉由被糾氣體而成減壓狀態。若室 則滾筒29與剝離輥33之間的第2= 被,,能夠設成比第1空間更低的勤。J工間也 ί (第2圖中用座線表示的符號Α)變為::徑 ^以使朝向剝離镜33的濕_16靠近室55,為曲線路 圖從側方觀察時,傭 侧’如第2 路徑控制部36為吸引.衷凸形狀。如此, 的氣體之糊第2空間 _33之間的第2空間進行減昼二 201132686 37782pif 路在第2空間側成為凸形狀。 藉由使濕潤膜16之傳送路在第2空間侧成為凸形 ^ 了剝離而向濕潤膜16賦予的力中施加在濕潤膜^ 長邊方向的力比以往更大幅減小,從而能夠將所賦予 中更多的力用於剝離。因此,濕潤膜16的聚合物的、 膜面的方向上的取向(以下稱為面取向)得到抑制,= 加工適性和返工性均得以提高。 。禾 昧右方Γ,若剝離時的力過大則濕潤膜16在剝離 夺有可此被切。越使製造速度加快,祕_溶劑 率越两’故而流延膜32與滾筒29之黏附性更大。因=留 越使製膜速度加快_時的力變得越A,因此也容 割、。與此相對,根據本發明的上述方法,由於在一定 ^度下㈣進-步減小爲了剝離而賦予的力,由此处果 還有能夠進-步增大製造速度之類的效果。並且,根= 述方法,不實施對剛剝離後的溶劑殘留率非常高的渴 16=氣體噴吹,因此在維持_膜16⑽面的平滑、 同時’能夠避免由異物引起的污染。 ’ 如以上,藉由控制朝向剝離輥3 3的濕潤膜! 6 ^ ’能夠使剝離位置PP中滾筒29的周s祝與濕潤膜 1所成的角Θ1變大’故而容易較低地控糊離所需的力。、 ^ Γί為剝離位置PP中滾筒29的周面29a與濕潤膜16 所成的角Θ1設為30。以上80。以下的範圍。 所剝離位置pp中滾筒29的周面29a與濕潤膜16 所成的角Θ1變大,則相對於剝離親33的捲繞中心角θ2 15 201132686 37782pif 告各易較大地保持 之間的傳送路的形 變得大於直線路徑A時的捲繞中心角。 捲繞中心角Θ2’則滾筒29與剝離輥幻 狀也更加容易地保持為凸形狀。 繞在剝離親33 心構成的扇形 另外’捲繞中心角θ2係由濕潤膜16捲 的捲繞區域72與剝離輥33之斷面圓形的中 的中心角。 從進一步放大剝離位置ΡΡ中滾筒29 满膜16所成的角Θ1以及捲繞中心角;a濕 實施方式,較佳為❹_33不作為來看’如本 在第2空間側突出的傳送路徑的形狀 使其較大地突㈣,降低驅動輥之轉速即可言、祥,或 了僅由依室55的吸引進一步加大朝向剝離輥3二蟲: 16之傳送路徑的方法之外,亦可藉由將剝㈣μ =酿 動輕來進-步加大剝離位置ρρ中的滚筒29 ^為驅 濕潤膜16所成的角Θ1以及捲繞中心角的。° &與 本實施方式中,以第2空間更低於第丨空_ 方式進行龍,但本發明並不局限於此。例如 = 了第2空間的減壓,也可以對第i ^間進行加壓。其 該加壓並非祕壓下的加壓,岐靜壓下的加壓/、’ 壓下的加壓能夠藉由反復進行如下送人操作和停止 2作來進行’前述送入操作以包括滾筒29的下游側的一 =和剝離3 3的上游側的一部份的方式由室(未圖; 圍第1空間和濕潤膜16之直線路徑Α,並以一定的時間 該至内送入氣體;前述停止操作以一定時間停止送入 201132686 s//}SZpit 作。依該方法,能夠大幅抑制氣體之噴吹之類的動壓之發 生’並且能夠從第1空間側向濕潤膜16賦予壓力。又,在 將滾琦29與剝離輥33之間設為數mm程度的極小間隙 時,如果依該方法也能夠確實地對第1空間和第2空間賦 予壓力差。並且,比起從在寬度方向Z2上延伸的狹縫狀 的開口吸引氣體,更能確實地保持膜面的平滑性。 并馮用於向滾筒29與剝離輥33為止的第}空間與第 2空間設置壓力差的方法,還有其他方法。例如有如下方 法··不使用室55或包圍第1空間和濕潤膜16之直線路徑 A的上述室(未圖示)而配設包圍膜形成裝置17 (參照^ 1圖)的整體的室(未圖示),在其中,設置隔開内部空 力差。藉由分別控制由隔開構件开^ 空間之壓力,能夠對比濕_ 16之傳送路更靠“ 間和更#近下方的第2空_傾力差。當滚 為利用為麵㈣以上時,進一步較佳 mi 解'"壓力差。當滾筒29與剝離輥33之距離 =5 〇〇卿時’亦可為如下方法:不使用室55或包圍; 1空間和濕_ 16之直線路徑 =圍第 設包圍膜形成裝置17(i # 31至(未圖不)而配 ^ (參照第1圖)整體的室(未圖示), 用^開構件將其中隔開來辦予該壓力差。 ) 較佳為第1空間斑第2办 通過剝_33中捲繞間之壓力差依從剝離位置冲 決定。較佳為溶劑殘留賴膜16之溶劑殘留率 一步較大地突出。這是因為、ί越加大壓力差而使傳送路進 口為〉谷劑殘留率越大,滚筒2 9與流 17= the first opening opposite the wet film 16. From this! J cited ^55 external gas. The plate-shaped i-th to fifth members 61 to =4 are arranged in an upright posture. The middle illusion 罘 罘 构件 i member 61 is disposed in consideration of the casting film 32 and is disposed at a distance from the drum 29 in the range of 25 (8) handsome to 13 201132686 37782pif. The conveying direction Z1 t& the downstream end 29D of the drum 4 is closer to the upstream. The target member 62 is changed to the distance from the peeling roller 33 in consideration of the click of the wet film 16 in the range of the predetermined degree. On the Z1, the 25GG division is lower than the upstream end 33Uf and the downstream end 62D of the peeling roller 33, and the gas inside the second formation is formed by the second opening: .69 Wei 56 connection' The third member 63 of the chamber and the side member 16e of the fourth member 64 are disposed closer to the outer side of the side member 16e. Thus, the climbing film 16 does not have a thirst with the third member 63 and the fourth member, and the wet film 16 pairs of sides of the ^ ^ side view like 'become the ridge, the marrow〗 〖Blood ~ way in the second picture, so it does not necessarily have to be the surface of the surface of the surface of the overlapping surface, but also within the ^Hi internal The gas is corrected to a reduced pressure state. If the second = between the chamber roller 29 and the peeling roller 33 is set, it can be set to be lower than the first space. The J workspace also ί (the symbol Α indicated by the seat line in Fig. 2) becomes: the diameter ^ so that the wet _16 toward the peeling mirror 33 is close to the chamber 55, and the curved road map is viewed from the side, the servant side 'The second path control unit 36 is a convex shape. In this way, the second space between the second space _33 of the gas paste is reduced by two. 201132686 The 37782pif path has a convex shape on the second space side. By causing the transport path of the wet film 16 to be convexly peeled off on the second space side, the force applied to the wet film 16 in the longitudinal direction of the wet film is more greatly reduced than in the related art. Give more force in the strip for peeling. Therefore, the orientation of the polymer of the wet film 16 in the direction of the film surface (hereinafter referred to as the plane orientation) is suppressed, and both the workability and the reworkability are improved. . On the right side of the sputum, if the force at the time of peeling is too large, the wet film 16 can be cut by peeling. The faster the manufacturing speed is, the more the secret solvent ratio is doubled, so that the casting film 32 and the roller 29 are more adhesive. Since the force at which the film forming speed is increased as the value of the filming speed is increased, the A becomes more, so it is also accommodated. On the other hand, according to the above method of the present invention, since the force applied for peeling is further reduced at a certain degree (four), there is an effect that the manufacturing speed can be further increased. Further, in the root method, since the thirst 16 = gas injection having a very high solvent residual ratio immediately after the peeling is not performed, the smoothness of the surface of the film 16 (10) is maintained, and contamination by foreign matter can be avoided. As above, by controlling the wetting film toward the peeling roller 3 3! 6 ^ ' can increase the angle Θ1 formed by the circumference s of the drum 29 in the peeling position PP and the wet film 1, so that it is easy to control the force required for the paste. And Γί is the angle Θ1 formed by the circumferential surface 29a of the drum 29 in the peeling position PP and the wet film 16 is set to 30. Above 80. The following range. When the angle Θ1 formed by the circumferential surface 29a of the drum 29 and the wet film 16 in the peeling position pp becomes larger, the winding center angle θ2 15 201132686 37782pif with respect to the peeling pro 33 is easily maintained. The winding becomes larger than the winding center angle when the straight path A is formed. The winding center angle Θ 2' also makes it easier to maintain the convex shape of the drum 29 and the peeling roller. The fan-shaped shape formed by the peeling of the pro-33 is additionally. The winding center angle θ2 is a central angle of the circular shape of the winding region 72 wound by the wet film 16 and the peeling roller 33. From the further enlargement of the peeling position ΡΡ, the angle Θ1 formed by the full film 16 of the drum 29 and the winding center angle; a wet embodiment, preferably ❹_33 does not serve as a view of the shape of the conveying path that protrudes on the second space side. The large protrusion (4), the rotation speed of the driving roller can be reduced, or it can be further increased by the suction of the chamber 55 to the conveying path of the second roller: 16 of the peeling roller 3, (4) μ = brewing lightly advances - the step of increasing the peeling position ρρ of the drum 29 ^ is the angle Θ 1 formed by the wetted film 16 and the winding center angle. ° & In the present embodiment, the dragon is performed in a manner that the second space is lower than the first hollow _, but the present invention is not limited thereto. For example, = decompression in the second space, or pressurizing the i-th. The pressurization is not the pressurization under the secret pressure, and the pressurization under the static pressure/, the pressurization of the press can be performed by repeating the following transfer operation and stop 2 to perform the aforementioned feeding operation to include the roller. A portion of the downstream side of 29 and a portion of the upstream side of the peeling 3 3 are formed by a chamber (not shown; a straight path surrounding the first space and the wet film 16 is entangled, and the gas is supplied therein at a certain time. The stop operation is stopped for a certain period of time and is sent to 201132686 s//} SZpit. According to this method, the occurrence of dynamic pressure such as gas injection can be greatly suppressed and pressure can be applied to the wet film 16 from the first space side. In addition, when the gap between the rolling sheet 29 and the peeling roller 33 is set to a minimum of several mm, the pressure difference can be surely applied to the first space and the second space by this method. The slit-shaped opening extending in the direction Z2 attracts the gas, and the smoothness of the film surface can be surely maintained. The method for providing a pressure difference between the first space and the second space to the roll 29 and the peeling roll 33 is used. There are other methods. For example, there are the following methods. A chamber (not shown) surrounding the membrane forming device 17 (see FIG. 1) is disposed in the chamber 55 or the chamber (not shown) surrounding the linear path A of the first space and the wet film 16 in the chamber (not shown). The gap between the internal air and the air force is set. By separately controlling the pressure of the space opened by the partitioning member, it is possible to compare the transmission path of the wet _ 16 with the second air _ tilting force difference between the lower and the lower. In order to utilize the surface (four) or more, the pressure difference is further improved. When the distance between the drum 29 and the peeling roller 33 is 5 〇〇 ', the following method may be used: the chamber 55 is not used or surrounded; The linear path of the wet _ 16 is a chamber (not shown) that surrounds the entire membrane forming device 17 (i # 31 to (not shown) and is equipped with (see Fig. 1), and is opened by a member. It is preferable to divide the pressure difference by the separation.) It is preferable that the first space spot 2 is determined by the pressure difference between the windings in the peeling _33 depending on the peeling position. It is preferable that the solvent residual ratio of the solvent residual film 16 is one step. Larger out. This is because, ί increases the pressure difference and makes the transfer path inlet the larger the residual rate of the grain, the roller 2 9 And stream 17
201132686 3//82piI 延膜32之黏附力越強,並且濕潤膜16越容易破裂。 剝離位置PP越朝向寬度方向Z2上的中央,越在滾筒 29的旋轉方向上的下游側形成。因此,剝離時向濕潤膜16 之長邊方向賦予的力越朝向寬度方向Z2上的中央越變 大,且面取向越變大。因此,進一步較佳為在剝離位置pp 中,使第2空間的壓力隨著朝向中央靠近而變低。由此, 能夠製造出面取向在寬度方向Z2上一定的膜23。為了使 第2空間的壓力隨著朝向剝離位置pp的中央而變低,例 如在室55之内部進一步設置獨立的室(未圖示)而獨立控 制該室和室55之各内部壓力之方法。 當聚合物11 (參照第1圖)為纖維素醯化物時,本發 明尤其有效。 以下a己载了作為本發明之實施例和與本發明相對的比 較例。 [實施例1] 用冷部凝膠化流延方式製造膜23。在濕潤膜形成裝置 17之内部設置隔開構件(未圖示)以使對第丨空間和第2 空間賦予壓力差。對第1空間加壓而使其壓力比大氣壓高 1广,並使濕顧16之傳送路在第2空間成為凸形狀。另 2第2空間之壓力與大氣壓相等。隨此,使滾筒29與和 I制链33之速度比變化’以使剝離位置即成為怪定,從 *造膜另外,表1中“第1空間之壓力(Pa),,和“第 二間之壓力(Pa) ’’的各儀數值是以大氣壓為基準的 值。亦即’將壓力等於大氣壓的情況記載為0 (零),高於 201132686 •ί//δ2ριΐ· 大氣壓的情況記載為正值,低於大氣壓的情況記載為負值。 關於得到的膜23,根據以下方法及基準評價了加工適 性和返工性。其結果如表1所示。 (一) 加工適性 透過黏接劑將得到的膜23重疊黏接在偏光膜之兩 面,製作出偏光板。用刀具將偏光板沖壓成1〇cmxl〇cm之 矩形,作為評價用樣品。評價從該評價用樣品之長邊邊緣 亦即切割面到膜23之内部是否發生裂紋,對被確認的裂紋 的程度依如下基準進行加工適性評價。裂紋有時是從膜23 之切割面朝向内部的破損’也有時為偏光膜與膜23之間的 脫落。依如下基準,A〜C為加工適性合格的水平,D為 加工適性不合格的水平。 卜A:看不到裂紋,或者雖然發生裂紋,但發生的裂紋 範圍控制在不到長邊的長度的25%。 B ·發生裂紋的範圍控制在長邊之長度的25%以上不 到50%的範圍。 C:發生裂紋的範圍控制在長邊的長度的5〇%以上不 到75%的範圍。 D .發生裂紋的範圍在長邊的長度的75%以上。 (二) 返工性201132686 3//82piI The stronger the adhesion of the film 32, and the more easily the wet film 16 is broken. The peeling position PP is formed toward the center in the width direction Z2, and is formed on the downstream side in the rotation direction of the drum 29. Therefore, the force applied to the longitudinal direction of the wet film 16 at the time of peeling becomes larger toward the center in the width direction Z2, and the surface orientation becomes larger. Therefore, it is more preferable that the pressure in the second space is lowered toward the center in the peeling position pp. Thereby, the film 23 whose surface orientation is constant in the width direction Z2 can be manufactured. In order to lower the pressure in the second space toward the center of the peeling position pp, for example, a separate chamber (not shown) is provided inside the chamber 55 to independently control the internal pressures of the chamber and the chamber 55. The present invention is particularly effective when the polymer 11 (refer to Fig. 1) is a cellulose halide. The following a has been carried out as an embodiment of the present invention and a comparative example to the present invention. [Example 1] A film 23 was produced by a cold portion gelation casting method. A partition member (not shown) is provided inside the wet film forming apparatus 17 to apply a pressure difference to the second space and the second space. The first space is pressurized so that the pressure is wider than the atmospheric pressure, and the transport path of the wet 16 is convex in the second space. The pressure in the other 2nd space is equal to the atmospheric pressure. Accordingly, the speed ratio of the drum 29 to the I chain 33 is changed so that the peeling position becomes strange, and the film is formed from *, and the pressure (Pa) of the first space, and "second" in Table 1 The value of each pressure (Pa) '' is based on atmospheric pressure. That is, the case where the pressure is equal to the atmospheric pressure is described as 0 (zero), and the case where the pressure is higher than 201132686 • ί//δ2ριΐ· atmospheric pressure is described as a positive value, and the case where the pressure is lower than the atmospheric pressure is described as a negative value. Regarding the obtained film 23, processing suitability and reworkability were evaluated according to the following methods and criteria. The results are shown in Table 1. (I) Processing suitability The obtained film 23 was adhered to both sides of the polarizing film by an adhesive to form a polarizing plate. The polarizing plate was punched into a rectangle of 1 〇 cm x 1 〇 cm with a cutter as a sample for evaluation. It was evaluated whether or not cracks occurred from the long side edge of the sample for evaluation, that is, the cut surface to the inside of the film 23, and the degree of the crack to be confirmed was evaluated for the suitability according to the following criteria. The crack may be broken from the cut surface of the film 23 toward the inside, and may be peeled off between the polarizing film and the film 23. According to the following criteria, A to C are the levels of acceptable processing suitability, and D is the level of unsuitable processing suitability. A: No crack is observed, or although cracking occurs, the crack range that occurs is controlled to be less than 25% of the length of the long side. B. The range in which cracks occur is controlled within a range of 25% or more of the length of the long side and less than 50%. C: The range in which the crack occurs is controlled in the range of 5 % or more of the length of the long side and not more than 75%. D. The range in which cracks occur is 75% or more of the length of the long side. (ii) Rework
透過黏接劑將得到的膜23重疊黏接在偏光膜之兩 面製作出偏光板。將偏光板貼合在玻璃基板之後,從破 璃基板剝下來。目視確認玻璃基板上的、膜的殘留脫落 的程度,依如下基準評價返工性。並依如下基準,A〜C 201132686 ο / /οζριι 為返工性合格的水平,D為返工性不合格的水平。 A:完全未確認到殘留脫落。 B:有極少殘留脫落的程度。 C:雖然有極少的殘留脫落,但在實用上沒有問 程度。 D:有很多殘留脫落。 [實施例2] 在濕潤膜形成裝置17之内部設置隔開構件(未圖干 以使對第1空間和第2空間賦予壓力差。對第2空間 減壓而使其壓力比大氣壓力低lGPa,並使濕潤膜^ ^ 送路在第2空間侧成為凸形狀。另外,第1空間之壓力與 大氣壓力相等。其他與實施例1相同。 ' [實施例3] 以利用第1圖所示之溶液製膜設備,亦即,第2圖的 路徑控制部36的形態,對第2空間進行減壓而使其壓力比 大氣壓低30Pa。亦即,從第2空間之壓力P2減去等於大 氣壓的第1空間之壓力P1的差壓P2-P1為_301^,這樣藉 由設置差壓來使濕潤膜16之傳送路在第2空間侧成為凸形 狀。剝離親33為驅動輥。隨此,調整滾筒29與剝離輥33 的旋轉的速度比以使剝離位置PP成為恆定,從而製造膜 23 ° [實施例4] 利用路徑控制部36使第2空間比起第1空間進一步減 壓(差壓P2-P1為-l〇〇Pa),使濕潤膜16之傳送路在第2 201132686 J//82pit 空間侧成為凸形狀’令Θ1為80。。第1空間之壓力與大氣 壓相等。除此之外與實施例3相同地實施。 [實施例5] 利用路徑控制部36使第2空間比起第1空間進一步滅 壓(差壓Ρ2-Ρ1為-30Pa)’使濕潤膜16之傳送路在第2空 間側成為凸形狀。第1空間之壓力与大氣壓相等。使滚筒 29和剝離輥33之各速度變化從而調整兩者的速度比,以 使剝離位置PP中滾筒29的周面29a和濕潤膜16所成的 角Θ1為30°。除此之外與實施例3相同地實施。 [實施例6] 利用路徑控制部36使第2空間比起第1空間進一步減 壓(差壓P2-P1為-30Pa)’使濕潤膜16之傳送路在第2空 間側成為凸形狀。第1空間之壓力与大氣壓相等。使滾筒 29和剝離輥33之各速度變化從而調整兩者的速度比,以 使剝離位置PP中滾筒29之周面29a和濕潤膜16所成的 角Θ1為80°。除此之外與實施例3相同地實施。 [實施例7] 利用路徑控制部36使第2空間比起第1空間進一步減 壓(差壓P2-P1為-30Pa)’使濕潤膜16之傳送路在第2空 間側成為凸形狀。第1空間之壓力与大氣壓相等。使滾筒 29和剝離輥33之各速度變化從而調整兩者的速度比,以 使剝離位置PP中滾筒29的周面29a和濕潤膜16所成的 角Θ1為90°。除此之外與實施例3相同地實施。 [比較例] 21 201132686 j//»zpit 從第1圖之溶液製膜設備10卸下路徑控制部36的狀 態下,用冷卻凝膠化流延方式製造膜。第1空間及第2空 間之壓力差為0 (零),從滚筒29朝向剝離輥33之濕潤膜 的傳送路徑如第2圖的符號A所示為直線路徑。使滚筒29 和剝離輥33之各速度變化來調整兩者的速度比,以使剝離 位置PP中滾筒29之周面29a和濕潤膜所成的角Θ2為30°。 有關在實施例2〜實施例7得到的各膜23和在由比較 例中得到的膜依與實施例1相同的方法及標準分別評價加 工適性和返工性。 22 201132686 ^//δζρΐΐThe obtained film 23 was adhered to both sides of the polarizing film by an adhesive to form a polarizing plate. After the polarizing plate is attached to the glass substrate, it is peeled off from the glass substrate. The degree of residual peeling of the film on the glass substrate was visually observed, and the reworkability was evaluated according to the following criteria. And according to the following criteria, A~C 201132686 ο / /οζριι is the level of reworkability, and D is the level of rework failure. A: No residue was observed at all. B: There is little degree of residual shedding. C: Although there is little residual shedding, there is no practical degree of application. D: There is a lot of residue falling off. [Embodiment 2] A partition member is provided inside the wet film forming apparatus 17 (not shown so as to apply a pressure difference to the first space and the second space. The second space is depressurized so that the pressure is lower than the atmospheric pressure by 1 GPa. And the wet film is formed in a convex shape on the second space side. The pressure in the first space is equal to the atmospheric pressure. Others are the same as in the first embodiment. [Example 3] The solution film forming apparatus, that is, the path control unit 36 of Fig. 2, decompresses the second space so that the pressure is 30 Pa lower than the atmospheric pressure, that is, the pressure P2 of the second space is equal to the atmospheric pressure. The differential pressure P2-P1 of the pressure P1 in the first space is _301^, and the differential pressure is applied to make the transport path of the wet film 16 convex on the second space side. The peeling pro 33 is a driving roller. By adjusting the speed ratio of the rotation of the drum 29 and the peeling roller 33 so that the peeling position PP is constant, the film 23 is produced. [Example 4] The second space is further decompressed by the path control unit 36 than the first space (difference The pressure P2-P1 is -l〇〇Pa), so that the transmission path of the wet film 16 is at the second 201132686 J//82p The space side has a convex shape and the Θ1 is 80. The pressure in the first space is equal to the atmospheric pressure. The fifth embodiment is similar to the third embodiment. [Embodiment 5] The second space is compared with the path control unit 36. The first space is further decompressed (differential pressure Ρ2-Ρ1 is -30 Pa). The transport path of the wet film 16 is convex on the second space side. The pressure in the first space is equal to the atmospheric pressure. The drum 29 and the peeling roller 33 are The speed ratio of each of the speeds was adjusted so that the angle Θ1 formed by the circumferential surface 29a of the drum 29 and the wet film 16 in the peeling position PP was 30°. The same procedure as in the third embodiment was carried out. (Example 6) The path control unit 36 further decompresses the second space from the first space (the differential pressure P2-P1 is -30 Pa). The transfer path of the wet film 16 is convex on the second space side. The pressure is equal to the atmospheric pressure, and the respective speeds of the drum 29 and the peeling roller 33 are changed to adjust the speed ratio of the both, so that the angle Θ1 formed by the circumferential surface 29a of the drum 29 and the wet film 16 in the peeling position PP is 80°. Except for this, it is carried out in the same manner as in the third embodiment. [Embodiment 7] The path control unit 36 is used. 2 The space is further decompressed than the first space (the differential pressure P2-P1 is -30 Pa). The transfer path of the wet film 16 is convex on the second space side. The pressure in the first space is equal to the atmospheric pressure. The respective speeds of the peeling rolls 33 are changed to adjust the speed ratio of the both, so that the angle Θ1 formed by the circumferential surface 29a of the drum 29 and the wet film 16 in the peeling position PP is 90°. Otherwise, the same as in the third embodiment. [Comparative Example] 21 201132686 j//»zpit The film was produced by a cooling gelation casting method in a state where the path control unit 36 was removed from the solution film forming apparatus 10 of Fig. 1 . The pressure difference between the first space and the second space is 0 (zero), and the transport path from the drum 29 toward the wet film of the peeling roller 33 is a straight path as indicated by the symbol A in Fig. 2 . The respective speeds of the drum 29 and the peeling roller 33 were changed to adjust the speed ratio of the both, so that the circumferential surface 29a of the drum 29 and the angle Θ2 formed by the wet film in the peeling position PP were 30°. The film 23 obtained in each of Examples 2 to 7 and the film obtained in the comparative example were evaluated for workability and reworkability, respectively, according to the same methods and standards as in Example 1. 22 201132686 ^//δζρΐΐ
[表Γ 第1空間之 壓力 第2空間之 壓力 有無室 55 Θ1 力口工適 性 返工性 (對大氣壓) (對大氣壓) (Pa) (Pa) (。) 實施例1 10 0 無 50 B p> 實施例2 0 -10 無 50 B L B r> 實施例3 0 -30 有 65 B B 實施例4 0 -100 有 80 Δ A 實施例5 0 -30 有 30 r> A 實施例6 0 -30 有 80 ο —-----— Δ -~~§_ 實施例7 0 -30 有 90 r\. 一 一 c A 比較例 _______0_ 0 無 30 D c D 太私日^發明已以實關揭露如上,然其並非用以限定 任何㈣技術領域巾具有通常知識者,在不脫離 發月之精神和範_,#可作些許之更動與潤飾 3明之保護範圍當視後附之t請專利範n所界定者為車 【圖式簡單說明】 々平。 圖1是已實施本發明的溶液製膜設備的簡要圖。 圖2是路徑控制部之簡要圖。 圖3是路徨控制部之簡要圖。 23 201132686 »/ / / 【主要元件符號說明】 10 :溶液製膜設備 16 :濕潤膜 17 :濕潤膜形成裝置 23 :膜 29 :滚筒 32 :流延膜 33 :剝離輥 36 :路徑控制部 55 :室 72 :捲繞區域 24[Table 压力 Pressure of the first space Pressure of the second space with or without chamber 55 Θ1 Workability of rework (to atmospheric pressure) (for atmospheric pressure) (Pa) (Pa) (.) Example 1 10 0 No 50 B p> Example 2 0 - 10 No 50 BLB r > Example 3 0 -30 65 BB Example 4 0 - 100 80 Δ A Example 5 0 -30 There are 30 r > A Example 6 0 -30 There are 80 ο ---------- Δ -~~§_ Example 7 0 -30 has 90 r\. 一一c A Comparative example _______0_ 0 No 30 D c D Too private day ^Invention has been revealed as above, However, it is not intended to limit any (4) technical field towels with the usual knowledge, without departing from the spirit of the moon and the scope of the _, # can make some changes and refinement 3 Ming's protection scope is attached to the t-recognition patent For the car [simple description of the map] 々平. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic view of a solution film forming apparatus in which the present invention has been carried out. 2 is a schematic diagram of a path control unit. Fig. 3 is a schematic diagram of a road control unit. 23 201132686 »/ / / [Description of main component symbols] 10 : Solution film forming apparatus 16 : Wetting film 17 : Wetting film forming apparatus 23 : Film 29 : Roller 32 : Cast film 33 : Peeling roll 36 : Path control part 55 : Chamber 72: Winding area 24
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2010062556A JP5466056B2 (en) | 2010-03-18 | 2010-03-18 | Solution casting method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| TW201132686A true TW201132686A (en) | 2011-10-01 |
| TWI491651B TWI491651B (en) | 2015-07-11 |
Family
ID=44599745
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW100108765A TWI491651B (en) | 2010-03-18 | 2011-03-15 | Solution casting method |
Country Status (4)
| Country | Link |
|---|---|
| JP (1) | JP5466056B2 (en) |
| KR (1) | KR101808340B1 (en) |
| CN (1) | CN102190809B (en) |
| TW (1) | TWI491651B (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5404497B2 (en) * | 2010-03-30 | 2014-01-29 | 富士フイルム株式会社 | Solution casting method |
| JP5441995B2 (en) * | 2011-03-29 | 2014-03-12 | 富士フイルム株式会社 | Solution casting method |
| JP6346579B2 (en) * | 2015-03-09 | 2018-06-20 | 富士フイルム株式会社 | Solution casting method |
| JP6586787B2 (en) * | 2015-06-18 | 2019-10-09 | コニカミノルタ株式会社 | Manufacturing method of resin film |
Family Cites Families (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS51137465U (en) * | 1975-04-30 | 1976-11-06 | ||
| JPS6264514A (en) * | 1985-09-17 | 1987-03-23 | Fuji Photo Film Co Ltd | Manufacture of cellulose triacetate film |
| JP3931514B2 (en) * | 2000-01-18 | 2007-06-20 | コニカミノルタホールディングス株式会社 | Method for producing cellulose acylate film |
| JP4128327B2 (en) * | 2000-12-22 | 2008-07-30 | 富士フイルム株式会社 | Method for producing optical use film |
| JP4400770B2 (en) * | 2001-02-28 | 2010-01-20 | 富士フイルム株式会社 | Solution casting method |
| JP4017139B2 (en) * | 2001-12-11 | 2007-12-05 | 富士フイルム株式会社 | Solution casting method |
| JP2003291160A (en) * | 2002-03-29 | 2003-10-14 | Fuji Photo Film Co Ltd | Solution film making method, cellulose ester film, protective film, and polarizing plate |
| JP4217119B2 (en) | 2003-07-17 | 2009-01-28 | 富士フイルム株式会社 | Solution casting equipment and method |
| JP4289615B2 (en) * | 2004-03-29 | 2009-07-01 | 富士フイルム株式会社 | Solution casting method and polymer film |
| JP4610507B2 (en) * | 2005-03-28 | 2011-01-12 | 富士フイルム株式会社 | Solution casting method |
| JP2008291204A (en) * | 2006-09-29 | 2008-12-04 | Fujifilm Corp | Cyclic polyolefin resin film and manufacturing method thereof, polarizing plate and liquid crystal display device |
-
2010
- 2010-03-18 JP JP2010062556A patent/JP5466056B2/en active Active
-
2011
- 2011-03-14 KR KR1020110022390A patent/KR101808340B1/en not_active Expired - Fee Related
- 2011-03-15 TW TW100108765A patent/TWI491651B/en not_active IP Right Cessation
- 2011-03-18 CN CN201110066287.4A patent/CN102190809B/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP5466056B2 (en) | 2014-04-09 |
| KR20110105342A (en) | 2011-09-26 |
| CN102190809A (en) | 2011-09-21 |
| JP2011194660A (en) | 2011-10-06 |
| CN102190809B (en) | 2015-01-14 |
| KR101808340B1 (en) | 2017-12-12 |
| TWI491651B (en) | 2015-07-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5404497B2 (en) | Solution casting method | |
| JP4607779B2 (en) | Method for producing polymer film | |
| TW201132686A (en) | Solution casting method | |
| TW201217139A (en) | Casting device and solution casting method | |
| JP4289615B2 (en) | Solution casting method and polymer film | |
| US9022097B2 (en) | Method and installation for manufacturing thin metal strip | |
| JP2004098512A (en) | Method for producing film from solution | |
| CN104890171B (en) | Casting device, solution film-forming device and method | |
| CN106965361B (en) | The manufacturing method of optical film | |
| CN103709423B (en) | Solution film-forming method | |
| TWI581934B (en) | Solution casting method | |
| JP5441995B2 (en) | Solution casting method | |
| TW201412489A (en) | Solution casting method | |
| JP5351477B2 (en) | Method for producing porous film | |
| KR102210074B1 (en) | Solution film-forming apparatus and method | |
| JP2010082993A (en) | Method of solution film-forming | |
| JP2007210344A (en) | Solution casting method | |
| KR102148042B1 (en) | Casting apparatus, solution film forming facility and method | |
| JP3978533B2 (en) | Film manufacturing method | |
| JP2000239403A (en) | Preparation of cellulose acylate film and cellulose acylate film | |
| WO2018061803A1 (en) | Solution film-forming method | |
| JP6737270B2 (en) | Method for manufacturing optical film | |
| JP2011202068A (en) | Solution film-forming method | |
| JP2009214388A (en) | Solution filming method | |
| JP2002248680A (en) | Method for stretching film made of solution |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MM4A | Annulment or lapse of patent due to non-payment of fees |