WO2014087872A1 - 延伸フィルムの製造方法 - Google Patents
延伸フィルムの製造方法 Download PDFInfo
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- WO2014087872A1 WO2014087872A1 PCT/JP2013/081702 JP2013081702W WO2014087872A1 WO 2014087872 A1 WO2014087872 A1 WO 2014087872A1 JP 2013081702 W JP2013081702 W JP 2013081702W WO 2014087872 A1 WO2014087872 A1 WO 2014087872A1
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- roll
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Classifications
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- 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
- B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
- B29C55/02—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
- B29C55/04—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets uniaxial, e.g. oblique
- B29C55/06—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets uniaxial, e.g. oblique parallel with the direction of feed
Definitions
- the present invention relates to a method for producing a stretched film, particularly a stretched film for optical applications.
- Such an optical film is required to have excellent transparency and excellent adhesiveness such as a coating layer for processing during prism lens processing, hard coating processing, and AR processing. It is desired that there are as few defects as possible.
- Patent Document 1 discloses a method for improving handling properties (e.g., slipperiness, winding property, blocking resistance) and scratch resistance of a film.
- Patent Document 2 discloses that a surfactant having a film surface has a length of 20 mm or more and a maximum depth of 0.5 ⁇ m or more of 10 scratches / m 2 or less.
- a polyester-based optical film is disclosed. However, it is difficult to suppress the generation of finer scratches and does not satisfy the level required for recent optical films.
- the present invention provides a method for producing a stretched film that is excellent in transparency, has few scratches, is suitable for various processing applications, and is suitable for optical applications.
- the upstream nip roll is the 0th nip roll and the downstream nip roll is the first nip roll.
- the portion sandwiched between the first stretching roll and the 0th nip roll is the 0th gripping portion and the portion sandwiched between the first stretching roll and the 1st nip roll is the first gripping portion
- the position of the 0th gripping part is the upstream end in the contact area between the film and the first stretching roll, and the position of the first gripping part is downstream in the contact area between the film and the first stretching roll.
- the method for producing a stretched film according to 1) wherein the stretched film is an end portion of the stretched film.
- the position of the second gripping part is the upstream end in the contact area between the film and the second stretching roll, and the position of the third gripping part is downstream in the contact area between the film and the second stretching roll.
- the 0th nip roll has a cleaning mechanism (hereinafter referred to as a first cleaning mechanism),
- the method for producing a stretched film according to any one of claims 1 to 4, wherein the first cleaning mechanism can clean the first transport roll located on the upstream side of the first stretch roll.
- the production method of the stretched film of the present invention can suppress the generation of scratches, and can provide a film with reduced defects, particularly optical defects, due to the scratches.
- the film in the present invention is not particularly limited, but means a thermoplastic resin film.
- thermoplastic resin film is not particularly limited, but as a typical example, polyethylene terephthalate, polyethylene-2, 6-naphthalate, nylon-6, polyphenylene sulfide and the like are preferably used.
- particle-containing pellets or pellets substantially free of particles are prepared using raw materials such as polyethylene terephthalate as described above.
- a pellet containing no particles is preferable in order to ensure transparency.
- a stretched film can be obtained by sequentially biaxially stretching such an unoriented polyester film in the film longitudinal direction and the width direction.
- the present invention is a process of longitudinally stretching a film using an upstream stretching roll (hereinafter referred to as a first stretching roll) and a downstream stretching roll (hereinafter referred to as a second stretching roll) (hereinafter, referred to as “first stretching roll”).
- first stretching roll an upstream stretching roll
- second stretching roll a downstream stretching roll
- first stretching roll a stretching roll
- This is a method for producing a stretched film including a longitudinal stretching step). That is, in the present invention, it is important to use two stretching rolls for performing the longitudinal stretching treatment.
- the heating temperature immediately before the first stretching roll is preferably 68 to 83 ° C., more preferably 70 to 80 ° C., and further preferably 72 to 75 ° C.
- the heating temperature immediately before the first stretching roll is lower than 68 ° C., the film tends to break, and when it is higher than 83 ° C., the film sticks to the roll and surface defects may easily occur.
- FIG. 1 shows only one embodiment, and the present invention is not limited to this figure.
- the first stretching roll (5) and the second stretching roll (6) are arranged at a distance in order to stretch the film (7).
- the number of nip rolls adjacent to the first stretching roll is not particularly limited as long as it is 2 or more, but preferably 2 to 3 and particularly preferably 2. That is, according to FIG. 1, there are two nip rolls close to the first drawing roll, and among the two nip rolls close to the first drawing roll, the upstream nip roll is the zero nip roll and the downstream nip roll. Is the first nip roll, the 0th nip roll (1) and the first nip roll (2) are arranged in the vicinity of the first draw roll in order to hold the film in the first draw roll.
- stretching roll is an edge part of a downstream in the contact area of a film and a 1st extending
- the number of nip rolls adjacent to the second stretching roll is preferably 2 or more, more preferably 2 to 3, and particularly preferably 2. That is, according to FIG. 1, there are two nip rolls close to the second drawing roll, and among the two nip rolls close to the second drawing roll, the upstream nip roll is the second nip roll, and the downstream nip roll. Is the third nip roll, it is preferable that the second nip roll (3) and the third nip roll (4) are disposed in the vicinity of the second draw roll in order to grip the film in the second draw roll.
- the stretching tension cannot be sufficiently cut, and the second conveying roll (on the downstream side of the second stretching roll ( 13) The film may slip and scratches may occur.
- the position is the upstream end in the contact area between the film and the second stretching roll
- the position of the third gripping part is the downstream end in the contact area between the film and the second stretching roll. It is preferable. That is, according to FIG. 1, the position of the 3rd holding part which a 3rd nip roll hold
- stretching roll is an upstream edge part in the contact area
- the 0th nip roll has a cleaning mechanism (hereinafter referred to as a first cleaning mechanism), and the first cleaning mechanism can clean the first transport roll located on the upstream side of the first stretching roll. It is preferable that That is, according to FIG. 1, it is preferable that the 0th nip roll has the first cleaning mechanism (10) and can clean the first transport roll located on the upstream side of the first stretching roll. This is because, when the film is produced for a long time, the stretching roll may cause the generation of flaws, so that the generation of debris can be minimized by having a mechanism capable of cleaning without cutting the film.
- the third nip roll has a cleaning mechanism (hereinafter referred to as a second cleaning mechanism), and the second cleaning mechanism can clean the second transport roll located on the downstream side of the second stretching roll.
- a second cleaning mechanism it is preferable. That is, according to FIG. 1, it is preferable that the 3rd nip roll has a 2nd cleaning mechanism, and can clean the 2nd conveyance roll located in the downstream of a 2nd extending
- the film temperature during stretching in the longitudinal stretching step is, for example, 70 to 130 ° C, preferably 75 to 120 ° C, more preferably 80 to 110 ° C.
- the film temperature during stretching in the longitudinal stretching step is lower than 70 ° C, the film is likely to break, and when the film temperature during stretching is higher than 130 ° C, the polymer is difficult to be oriented and breaks when stretched in the width direction. It becomes easy to do.
- the film temperature during stretching in the longitudinal stretching step means the film temperature in the region between the first stretching roll and the second stretching roll.
- the draw ratio in the longitudinal drawing step is, for example, 2.5 to 5.0 times, preferably 2.7 to 3.5 times.
- the longitudinal draw ratio is less than 2.5 times, it is difficult to obtain strength.
- the draw ratio in the longitudinal drawing step is more than 5.0 times, the orientation of the polymer is strong and the film is stretched in the width direction. Moreover, it becomes easy to break.
- the uniaxially stretched film obtained by the above method is, for example, 80 to 160 ° C., preferably 85 to 130 ° C., more preferably 90 to 120. It is possible to stretch the film in the width direction at a temperature of, for example, 2.5 to 6.0 times, preferably 3.0 to 5.5 times, more preferably 3.5 to 5.0 times. If the temperature and magnification range are out of the range, problems such as uneven stretching or film breakage may be caused. In particular, when the stretching temperature in the transverse stretching process is lower than 80 ° C., the film may be easily broken and the production may be difficult. On the other hand, if the stretching temperature in the transverse stretching process is higher than 160 ° C., sufficient strength may not be obtained for mold release.
- heat setting may be performed at 200 to 240 ° C., preferably 205 to 235 ° C., more preferably 210 to 230 ° C., followed by relaxation within 25%.
- the temperature at the time of heat setting is lower than 200 ° C., the crystallinity does not advance and the structure of the polyester may not be stable.
- a sheet-like sample (product width x 1 to 2 m) is taken from the surface of the film roll with a fixed winding length, and the number of scratches with a maximum major diameter of 500 ⁇ m or more is measured in a dark room under oblique light conditions. It was visually observed and converted into the number of scratches per 1 m 2 and ranked as follows.
- the polyethylene terephthalate pellets were dried at 160 ° C. for 8 hours, then fed to an extruder, melt extruded at 275 ° C. and filtered. Thereafter, the film was wound on a casting drum having a surface temperature of 25 ° C. by using an electrostatic application casting method on a cooling roll through a slit die kept at 285 ° C., and was cooled and individualized to obtain an unstretched film.
- the unstretched film was heated to 74 ° C. with a roll having a surface roughness Ra of 0.1 ⁇ m. And the film temperature at the time of extending
- first nip roll in the vicinity of the first stretching roll (there is only one nip roll in the vicinity of the first stretching roll), and the position of the first grip portion where the first nip roll grips the film is the first stretching roll and the film
- the second nip roll is in the downstream end of the area where the second nip roll contacts, and there is a second nip roll in the vicinity of the second drawing roll (there is only one nip roll in the vicinity of the second drawing roll), and the second nip roll holds the film.
- the position of the gripping part is located at the upstream end of the region where the second stretching roll and the film are in contact.
- stretching is performed while the film is heated with an infrared heater located between the first stretching roll and the second stretching roll. This method is called a basic longitudinal stretching method.
- Example 1 In addition to the above basic longitudinal stretching method, the 0th nip roll is provided in the vicinity of the 1st stretching roll, and the position of the 0th gripping portion where the 0th nip roll grips the film is in contact with the first stretching roll and the film.
- a stretching apparatus having a configuration located 30 ° downstream from the upstream endmost portion in the region was used, and the others were stretched in the longitudinal direction in the same manner as in the production example.
- this stretched film was introduced into a tenter, stretched 3.6 times in the width direction at a temperature of 100 ° C., and then heat treated at 225 ° C. with a constant width. Thereafter, a 6% relaxation treatment was further performed in the width direction to obtain a biaxially oriented polyester film having a thickness of 188 ⁇ m.
- Table 1 shows the number of scratches in the obtained stretched film. Table 1 also shows the number of scratches one day after production.
- Example 2 In the longitudinal stretching process of Example 1, biaxial stretching was performed in the same manner as in Example 1 except that the position of the 0th gripping portion was changed to the upstream end in the contact region between the first stretching roll and the film. A film was obtained.
- Example 3 In the longitudinal stretching step of Example 2, the third nip roll is provided near the second stretching roll, and the position of the third gripping portion where the third nip roll grips the film is determined in the contact region between the second stretching roll and the film.
- a biaxially stretched film was obtained in the same manner as in Example 2 except that the position was 30 ° upstream from the downstream end.
- Table 1 shows the number of scratches on the film obtained. Table 1 also shows the number of scratches one day after production.
- Example 4 In the longitudinal stretching process of Example 3, the position of the third gripping part was changed to the position of the downstream end in the contact area between the second stretching roll and the film, and the same as in Example 3, An axially stretched film was obtained.
- Example 5 In the longitudinal stretching step of Example 4, a biaxially stretched film was obtained in the same manner as in Example 4 except that the 0th nip roll had the first cleaning mechanism.
- Table 1 shows the number of scratches on the film obtained. In addition, Table 1 shows the level of the number of scratches one day after production, and the number level of scratches on the film obtained after cleaning the first transport roll using the first cleaning mechanism one day after production. Show.
- Comparative Example 1 there is one nip roll adjacent to the first stretching roll, and the portion sandwiched between the nip roll and the first stretching roll is the end on the downstream side in the contact area between the film and the first stretching roll. Therefore, in the table, the portion sandwiched between the nip roll and the first stretching roll is described as the first gripping portion.
- Example 1 and 2 and Comparative Example 1 the number of nip rolls adjacent to the second stretching roll is one, but the portion sandwiched between the nip roll and the second stretching roll is a contact area between the film and the second stretching roll.
- the portion sandwiched between the nip roll and the second stretching roll is described as the second gripping portion.
- the stretched film obtained by the production method of the present invention has the advantages of being excellent in transparency, having few scratches and being suitable for various processing applications. Therefore, various optical films, in particular, base films for prism sheets, hard coats. It is suitably used as a base film for reflection, a base film for antireflection (AR) film, a base film for light diffusion, a transparent conductive film, and the like.
- base films for prism sheets hard coats. It is suitably used as a base film for reflection, a base film for antireflection (AR) film, a base film for light diffusion, a transparent conductive film, and the like.
- AR antireflection
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Abstract
Description
1) 上流側の延伸ロール(以下、第1延伸ロールという)及び下流側の延伸ロール(以下、第2延伸ロールという)を用いて、フィルムに対して縦延伸処理を行う工程を含む延伸フィルムの製造方法において、
第1延伸ロールに近接するニップロールが、2本以上であることを特徴とする、延伸フィルムの製造方法。
2) 第1延伸ロールに近接するニップロールが2本であり、該第1延伸ロールに近接する2本のニップロールの中で、上流側のニップロールを第0ニップロール、下流側のニップロールを第1ニップロールとし、第1延伸ロール及び第0ニップロールに挟まれる部位を第0把持部、第1延伸ロール及び第1ニップロールに挟まれる部位を第1把持部とした際に、
第0把持部の位置が、フィルムと第1延伸ロールとの接触領域における、上流側の端部であり、第1把持部の位置が、フィルムと第1延伸ロールとの接触領域における、下流側の端部であることを特徴とする、1)に記載の延伸フィルムの製造方法。
3) 第2延伸ロールに近接するニップロールが、2本以上であることを特徴とする、1)又は2)に記載の延伸フィルムの製造方法。
4) 第2延伸ロールに近接するニップロールが2本であり、該第2延伸ロールに近接する2本のニップロールの中で、上流側のニップロールを第2ニップロール、下流側のニップロールを第3ニップロールとし、第2延伸ロール及び第2ニップロールに挟まれる部位を第2把持部、第2延伸ロール及び第3ニップロールに挟まれる部位を第3把持部とした際に、
第2把持部の位置が、フィルムと第2延伸ロールとの接触領域における、上流側の端部であり、第3把持部の位置が、フィルムと第2延伸ロールとの接触領域における、下流側の端部であることを特徴とする、1)~3)のいずれかに記載の延伸フィルムの製造方法。
5) 第0ニップロールが、清掃機構(以下、第1清掃機構という)を有し、
第1清掃機構は、第1延伸ロールの上流側に位置する第1搬送ロールを清掃可能であることを特徴とする、請求項1~4のいずれかに記載の延伸フィルムの製造方法。
6) 第3ニップロールが、清掃機構(以下、第2清掃機構という)を有し、
第2清掃機構は、第2延伸ロールの下流側に位置する第2搬送ロールを清掃可能であることを特徴とする、1)~5)のいずれかに記載の延伸フィルムの製造方法。
一定巻き長さのフィルムロール表層よりシート状のサンプル(製品幅×1~2m)を採取し、暗室において斜光の状態下で、キズの最大長径が500μm以上のキズ個数を目視にて観察し、1m2当たりのキズ個数に換算して、下記の通りランク分けを行った。
Aランク:50個/m2以下
Bランク:50個/m2より大きく75個/m2以下
Cランク:75個/m2より大きく100個/m2以下
Dランク:100個/m2より大きく120個/m2以下
Eランク:120個/m2より大きい(不合格)
上記判定基準中、Dランク以上のフィルムが実用上問題なく使用できるレベルであるが、Cランク以上が好ましい。
ポリエチレンテレフタレートのペレットを160℃で8時間乾燥した後、押出機に供給し、275℃で溶融押出しして濾過を行った。その後、285℃に保ったスリットダイを介し冷却ロール上に静電印加キャスト法を用いて表面温度25℃のキャスティングドラムに巻き付け冷却個化し、未延伸フィルムを得た。
上記基本的な縦延伸方法に加え、第1延伸ロール近傍には、第0ニップロールを有し、第0ニップロールがフィルムを把持する第0把持部の位置は、第1延伸ロールとフィルムとの接触領域における上流側最端部から30°下流側の位置にある構成の延伸装置を使い、その他については製造例と同様にして長手方向に延伸させた。
実施例1の縦延伸工程において、第0把持部の位置を、第1延伸ロールとフィルムとの接触領域における上流側の端部に変更したこと以外、実施例1と同様にして、二軸延伸フィルムを得た。
実施例2の縦延伸工程において、第2延伸ロール近傍に、第3ニップロールを有し、第3ニップロールがフィルムを把持する第3把持部の位置を、第2延伸ロールとフィルムとの接触領域における下流側の端部から30°上流側の位置になるようにしたこと以外、実施例2と同様にして、二軸延伸フィルムを得た。
実施例3の縦延伸工程において、第3把持部の位置を、第2延伸ロールとフィルムとの接触領域における下流側の端部の位置に変更したこと以外、実施例3と同様にして、二軸延伸フィルムを得た。
実施例4の縦延伸工程において、第0ニップロールに第1清掃機構を有する以外は、実施例4と同様にして、二軸延伸フィルムを得た。
実施例5の縦延伸工程において、第3ニップロールに第2清掃機構を有する以外は、実施例5と同様にして、二軸延伸フィルムを得た。
基本的な縦延伸方法で得られた二軸延伸フィルムのキズ個数レベル及び1日後生産した後のキズ個数レベルを表1に示す。
2 第1ニップロール
3 第2ニップロール
4 第3ニップロール
5 第1延伸ロール
6 第2延伸ロール
7 フィルム
8 第1接触領域
9 第2接触領域
10 第1清掃機構
11 第2清掃機構
12 第1搬送ロール
13 第2搬送ロール
Claims (6)
- 上流側の延伸ロール(以下、第1延伸ロールという)及び下流側の延伸ロール(以下、第2延伸ロールという)を用いて、フィルムに対して縦延伸処理を行う工程を含む延伸フィルムの製造方法において、
第1延伸ロールに近接するニップロールが、2本以上であることを特徴とする、延伸フィルムの製造方法。 - 第1延伸ロールに近接するニップロールが2本であり、該第1延伸ロールに近接する2本のニップロールの中で、上流側のニップロールを第0ニップロール、下流側のニップロールを第1ニップロールとし、第1延伸ロール及び第0ニップロールに挟まれる部位を第0把持部、第1延伸ロール及び第1ニップロールに挟まれる部位を第1把持部とした際に、
第0把持部の位置が、フィルムと第1延伸ロールとの接触領域における、上流側の端部であり、第1把持部の位置が、フィルムと第1延伸ロールとの接触領域における、下流側の端部であることを特徴とする、請求項1に記載の延伸フィルムの製造方法。 - 第2延伸ロールに近接するニップロールが、2本以上であることを特徴とする、請求項1又は2に記載の延伸フィルムの製造方法。
- 第2延伸ロールに近接するニップロールが2本であり、該第2延伸ロールに近接する2本のニップロールの中で、上流側のニップロールを第2ニップロール、下流側のニップロールを第3ニップロールとし、第2延伸ロール及び第2ニップロールに挟まれる部位を第2把持部、第2延伸ロール及び第3ニップロールに挟まれる部位を第3把持部とした際に、
第2把持部の位置が、フィルムと第2延伸ロールとの接触領域における、上流側の端部であり、第3把持部の位置が、フィルムと第2延伸ロールとの接触領域における、下流側の端部であることを特徴とする、請求項1~3のいずれかに記載の延伸フィルムの製造方法。 - 第0ニップロールが、清掃機構(以下、第1清掃機構という)を有し、
第1清掃機構は、第1延伸ロールの上流側に位置する第1搬送ロールを清掃可能であることを特徴とする、請求項1~4のいずれかに記載の延伸フィルムの製造方法。 - 第3ニップロールが、清掃機構(以下、第2清掃機構という)を有し、
第2清掃機構は、第2延伸ロールの下流側に位置する第2搬送ロールを清掃可能であることを特徴とする、請求項1~5のいずれかに記載の延伸フィルムの製造方法。
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CN201380063015.6A CN104822508B (zh) | 2012-12-04 | 2013-11-26 | 拉伸膜的制造方法 |
KR1020157011403A KR20150091302A (ko) | 2012-12-04 | 2013-11-26 | 연신 필름의 제조방법 |
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Cited By (1)
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WO2021037554A1 (de) | 2019-08-29 | 2021-03-04 | Saint-Gobain Glass France | Verfahren und vorrichtung zur herstellung einer thermoplastischen zwischenschichtfolie |
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US10137608B2 (en) * | 2016-09-20 | 2018-11-27 | Sumitomo Chemical Company, Limited | Film-stretching apparatus and method of producing film |
CN114643703A (zh) * | 2022-03-24 | 2022-06-21 | 江苏集萃功能材料研究所有限公司 | 一种薄膜拉伸系统及其应用 |
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JPS63134222A (ja) * | 1986-11-26 | 1988-06-06 | Kureha Chem Ind Co Ltd | ポリフエニレンスルフイドフイルムの縦延伸方法および装置 |
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JPS5829625A (ja) * | 1981-08-13 | 1983-02-21 | Teijin Ltd | 熱可塑性樹脂フイルムの延伸方法 |
JPS62214518A (ja) * | 1986-03-14 | 1987-09-21 | Diafoil Co Ltd | 磁気記録媒体用ポリエステルフイルム |
JP3520589B2 (ja) * | 1995-01-24 | 2004-04-19 | 東洋紡績株式会社 | 2軸配向ポリアミドフィルムの製造方法 |
JP4655381B2 (ja) * | 2001-02-22 | 2011-03-23 | 東レ株式会社 | ポリエステルフィルムの製造方法 |
AR038590A1 (es) * | 2002-02-22 | 2005-01-19 | Clopay Plastic Prod Co | Hoja laminada de pelicula y metodos para su fabricacion |
CN2629956Y (zh) * | 2003-06-18 | 2004-08-04 | 湖北力特土工材料有限公司 | 一种土工格栅拉伸装置 |
JP2010167768A (ja) * | 2008-12-22 | 2010-08-05 | Toyobo Co Ltd | 二軸延伸ポリエチレンテレフタレート系樹脂フィルムおよびその製造方法 |
JP5424717B2 (ja) * | 2009-05-29 | 2014-02-26 | 株式会社日本触媒 | 光学フィルムの製造方法 |
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- 2013-11-26 CN CN201380063015.6A patent/CN104822508B/zh active Active
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- 2013-11-26 WO PCT/JP2013/081702 patent/WO2014087872A1/ja active Application Filing
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JPS63134222A (ja) * | 1986-11-26 | 1988-06-06 | Kureha Chem Ind Co Ltd | ポリフエニレンスルフイドフイルムの縦延伸方法および装置 |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2021037554A1 (de) | 2019-08-29 | 2021-03-04 | Saint-Gobain Glass France | Verfahren und vorrichtung zur herstellung einer thermoplastischen zwischenschichtfolie |
EP4021723B1 (de) * | 2019-08-29 | 2023-09-27 | Saint-Gobain Glass France | Verfahren und vorrichtung zur herstellung einer thermoplastischen zwischenschichtfolie |
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JPWO2014087872A1 (ja) | 2017-01-05 |
TW201433594A (zh) | 2014-09-01 |
KR20150091302A (ko) | 2015-08-10 |
CN104822508B (zh) | 2017-10-10 |
CN104822508A (zh) | 2015-08-05 |
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